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Worldwide Engineering, Environmental, Construction, and IT Services
Equal Employment Opportunity Employer
6320 Rothway, Suite 100, Houston, Texas 77040
Telephone: (713) 734-3090 Fax: (713) 734-3391
www.CRAworld.com
May 19, 2015 Reference No. 082715
Mr. Jay Fedczak
Assistant Director for Permitting
Division of Air Quality
WV Department of Environmental Protection
601 57th Street, SE
Charleston, West Virginia 25304
Dear Mr. Jay Fedczak:
Re: General Permit Application G70-A
Edna Monroe Well Pad
Antero Resources Corporation
Conestoga-Rovers & Associates (CRA) would like to submit this General Permit application that
we prepared on behalf of Antero Resources Corporation for an oil and gas facility identified as
Edna Monroe Well Pad.
Enclosed are the following documents:
• Original copy of the G70-A General Permit Application
• Two CD copies of the G70-A General Permit Application
• The application fee with check no. 397724 in the amount of $1,500.00.
Please let us know if you have any questions or require additional information.
Sincerely,
CONESTOGA-ROVERS & ASSOCIATES
Manuel Bautista
Encl.
cc: Barry Schatz, Antero Resources Corporation
www.CRAworld.com
General Permit Application G70-A(New Facility)
Edna Monroe Well Pad
Prepared for: Antero Resources Corporation
Conestoga-Rovers & Associates6320 Rothway, Suite 100Houston, Texas 77040
May 2015 • 082715 • Report No. 197
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Table of Contents
G70-A General Permit Registration Form
Attachment A Current Business Certificate
Attachment B Process Description
Attachment C Description of Fugitive Emissions
Attachment D Process Flow Diagram
Attachment E Plot Plan
Attachment F Area Map
Attachment G Emission Unit Data Sheets/G70-A Section Applicability Form
Attachment H Air Pollution Control Device Data Sheet
Attachment I Emission Calculations
Attachment J Class I Legal Advertisement
Attachment K Electronic Submittal
Attachment L General Permit Registration Application Fee
Attachment M Siting Criteria Waiver
Attachment N Material Safety Data Sheets
Attachment O Emissions Summary Sheet
Attachment P Other Supporting Documentation (Engine EPA’s Certificate of Conformity and
Technical Information)
Page 1 of 5 Date of Last Application Revision 10/18/2013
WEST VIRGINIA
DEPARTMENT OF ENVIRONMENTAL PROTECTION
DIVISION OF AIR QUALITY
601 57th Street, SE
Charleston, WV 25304
Phone: (304) 926-0475 ٠ www.dep.wv.gov/daq
APPLICATION FOR GENERAL PERMIT REGISTRATION
CONSTRUCT, MODIFY, RELOCATE OR ADMINISTRATIVELY UPDATE
A STATIONARY SOURCE OF AIR POLLUTANTS
CONSTRUCTION MODIFICATION RELOCATION CLASS I ADMINISTRATIVE UPDATE
CLASS II ADMINISTRATIVE UPDATE
CHECK WHICH TYPE OF GENERAL PERMIT REGISTRATION YOU ARE APPLYING FOR:
G10-D – Coal Preparation and Handling
G20-B – Hot Mix Asphalt
G30-D – Natural Gas Compressor Stations
G33-A – Spark Ignition Internal Combustion Engines
G35-A – Natural Gas Compressor Stations (Flare/Glycol Dehydration Unit)
G40-C – Nonmetallic Minerals Processing
G50-B – Concrete Batch
G60-C – Class II Emergency Generator
G65-C – Class I Emergency Generator
G70-A – Class II Oil and Natural Gas Production Facility
SECTION I. GENERAL INFORMATION
1. Name of applicant (as registered with the WV Secretary of State’s Office):
Antero Resources Corporation
2. Federal Employer ID No. (FEIN):
80-0162034
3. Applicant’s mailing address:
1615 Wynkoop St. _________________________________________
Denver, CO, 80202 _________________________________________
4. Applicant’s physical address:
0.84 mile east from the intersection of Purgatory Run Rd.
(WV 30/1) and (Conaway Run Rd) WV 48
5. If applicant is a subsidiary corporation, please provide the name of parent corporation:
6. WV BUSINESS REGISTRATION. Is the applicant a resident of the State of West Virginia? YES NO
− IF YES, provide a copy of the Certificate of Incorporation/ Organization / Limited Partnership (one page) including any name change amendments or other Business Registration Certificate as Attachment A.
− IF NO, provide a copy of the Certificate of Authority / Authority of LLC / Registration (one page) including any name change amendments or other Business Certificate as Attachment A.
SECTION II. FACILITY INFORMATION
7. Type of plant or facility (stationary source) to be constructed, modified, relocated or administratively updated (e.g., coal preparation plant, primary crusher, etc.):
Natural Gas and Oil Production facility
8a. Standard Industrial AND 8b. North American Industry Classification
Classification (SIC) code: 1311 System (NAICS) code: 211111
9. DAQ Plant ID No. (for existing facilities only):
10. List all current 45CSR13 and other General Permit numbers associated with this process (for existing facilities only):
______________________________
_______________________________________
Page 2 of 5 Date of Last Application Revision 10/18/2013
A: PRIMARY OPERATING SITE INFORMATION
11A. Facility name of primary operating site:
Edna Monroe Well Pad_______________
12A. Address of primary operating site:
Mailing:__________N/A___________________ Physical: 0.84 mile east from the intersection of Purgatory Run Rd. (WV 30/1) and (Conaway Run Rd) WV 48
13A. Does the applicant own, lease, have an option to buy, or otherwise have control of the proposed site? YES NO − IF YES, please explain: _______Antero is leasing the mineral rights for this site________________________________________
____________________________________________________________________________________
− IF NO, YOU ARE NOT ELIGIBLE FOR A PERMIT FOR THIS SOURCE.
14A. − For Modifications or Administrative Updates at an existing facility, please provide directions to the present location of the facility from the
nearest state road;
− For Construction or Relocation permits, please provide directions to the proposed new site location from the nearest state road. Include a MAP as Attachment F.
From US 50W, turn right onto WV-18 N. Follow for 14.8 miles. Turn left onto Purgatory Run Rd and continue for 2.6 miles. Turn right onto Conaway Run Rd. The pad entrance will be 1.25 miles ahead on the left.
15A. Nearest city or town:
Middlebourne
16A. County:
Tyler
17A. UTM Coordinates:
Northing (KM): 4363.6852
Easting (KM): 510.916
Zone: 17 N
18A. Briefly describe the proposed new operation or change (s) to the facility:
New Natural Gas and Oil Production facility
19A. Latitude & Longitude Coordinates (NAD83, Decimal Degrees to 5 digits):
Latitude: 39.422626
Longitude: -80.873179
B: 1ST
ALTERNATE OPERATING SITE INFORMATION (only available for G20, G40, & G50 General Permits)
11B. Name of 1st alternate operating site:
____________________________________
____________________________________
12B. Address of 1st alternate operating site:
Mailing:_______________________________ Physical:_______________________________
_____________________________________________________________________________
13B. Does the applicant own, lease, have an option to buy, or otherwise have control of the proposed site? YES NO − IF YES, please explain: ____________________________________________________________________________________
____________________________________________________________________________________
− IF NO, YOU ARE NOT ELIGIBLE FOR A PERMIT FOR THIS SOURCE.
14B. − For Modifications or Administrative Updates at an existing facility, please provide directions to the present location of the facility from the
nearest state road;
− For Construction or Relocation permits, please provide directions to the proposed new site location from the nearest state road. Include a MAP as Attachment F.
___________________________________________________________________________________________________________
___________________________________________________________________________________________________________
___________________________________________________________________________________________________________
Page 3 of 5 Date of Last Application Revision 10/18/2013
15B. Nearest city or town:
16B. County: 17B. UTM Coordinates:
Northing (KM): ___________________
Easting (KM): ___________________
Zone: ___________________
18B. Briefly describe the proposed new operation or change (s) to the facility:
19B. Latitude & Longitude Coordinates (NAD83, Decimal Degrees to 5 digits):
Latitude: ___________________
Longitude: ___________________
C: 2ND
ALTERNATE OPERATING SITE INFORMATION (only available for G20, G40, & G50 General Permits):
11C. Name of 2nd
alternate operating site:
____________________________________
____________________________________
12C. Address of 2nd
alternate operating site:
Mailing:_______________________________ Physical:_______________________________
_____________________________________________________________________________
13C. Does the applicant own, lease, have an option to buy, or otherwise have control of the proposed site? YES NO − IF YES, please explain: ____________________________________________________________________________________
____________________________________________________________________________________
− IF NO, YOU ARE NOT ELIGIBLE FOR A PERMIT FOR THIS SOURCE.
14C. − For Modifications or Administrative Updates at an existing facility, please provide directions to the present location of the facility from the
nearest state road;
− For Construction or Relocation permits, please provide directions to the proposed new site location from the nearest state road. Include a MAP as Attachment F.
___________________________________________________________________________________________________________
___________________________________________________________________________________________________________
___________________________________________________________________________________________________________
15C. Nearest city or town:
16C. County: 17C. UTM Coordinates:
Northing (KM): ___________________
Easting (KM): ___________________
Zone: ___________________
18C. Briefly describe the proposed new operation or change (s) to the facility:
19C. Latitude & Longitude Coordinates (NAD83, Decimal Degrees to 5 digits):
Latitude: ___________________
Longitude: ___________________
20. Provide the date of anticipated installation or change:
01/01/2016
If this is an After-The-Fact permit application, provide the date upon which the proposed change did happen: :
_____/_____/_____
21. Date of anticipated Start-up if registration is granted:
02/16/2016
22. Provide maximum projected Operating Schedule of activity/activities outlined in this application if other than 8760 hours/year. (Note: anything other than 24/7/52 may result in a restriction to the facility’s operation).
Hours per day________ Days per week ________ Weeks per year ________ Percentage of operation ________
Page 4 of 5 Date of Last Application Revision 10/18/2013
SECTION III. ATTACHMENTS AND SUPPORTING DOCUMENTS
23. Include a check payable to WVDEP – Division of Air Quality with the appropriate application fee (per 45CSR22 and 45CSR13).
24. Include a Table of Contents as the first page of your application package.
All of the required forms and additional information can be found under the Permitting Section (General Permits) of DAQ’s website, or requested by phone.
25. Please check all attachments included with this permit application. Please refer to the appropriate reference document for an explanation of the attachments listed below.
ATTACHMENT A : CURRENT BUSINESS CERTIFICATE
ATTACHMENT B: PROCESS DESCRIPTION
ATTACHMENT C: DESCRIPTION OF FUGITIVE EMISSIONS
ATTACHMENT D: PROCESS FLOW DIAGRAM
ATTACHMENT E: PLOT PLAN
ATTACHMENT F: AREA MAP
ATTACHMENT G: EQUIPMENT DATA SHEETS AND REGISTRATION SECTION APPLICABILITY FORM
ATTACHMENT H: AIR POLLUTION CONTROL DEVICE SHEETS
ATTACHMENT I: EMISSIONS CALCULATIONS
ATTACHMENT J: CLASS I LEGAL ADVERTISEMENT
ATTACHMENT K: ELECTRONIC SUBMITTAL
ATTACHMENT L: GENERAL PERMIT REGISTRATION APPLICATION FEE
ATTACHMENT M: SITING CRITERIA WAIVER
ATTACHMENT N: MATERIAL SAFETY DATA SHEETS (MSDS)
ATTACHMENT O: EMISSIONS SUMMARY SHEETS
OTHER SUPPORTING DOCUMENTATION NOT DESCRIBED ABOVE (Equipment Drawings, Aggregation Discussion, etc.)
Please mail an original and two copies of the complete General Permit Registration Application with the signature(s) to the DAQ Permitting Section, at the address shown on the front page of this application. Please DO NOT fax permit applications. For questions regarding applications or West Virginia Air Pollution Rules and Regulations, please refer to the website shown on the front page of the application or call the phone number also provided on the front page of the application.
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment A
Current Business Certificate
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment B
Process Description
Antero Resources Corporation General Permit Application G70-A Edna Monroe Wellpad
082715 (197)
May 2015 B-1
Attachment B
Process Description
Edna Monroe Well Pad
Antero Resources Corporation
Tyler County, West Virginia
A mixture of condensate and entrained gas from the wells enters the facility through a number of three
phase low pressure separators where the gas phase is separated from the condensate and produced
water. Gas Processing Units (GPU) heaters (H001-H010) are used in conjunction with the separators to
help separate the gas from the liquid phases. These heaters are fueled by a slip stream of the separated
gas. The separated gas from the three phase low pressure separators is sent to a compressor (ENG001).
The compressed gas is then metered and sent to the sales gas pipeline. The separated water flow to the
produced water storage tanks (TANKPW001-002). The separated condensate is then sent to two phase
low pressure separators where gas is further separated from the condensate. The separated gas is
routed to the compressor (ENG001), compressed, sent to the sales gas line. The condensate from the
two phase separators flow to the condensate storage tanks (TANKCOND001-010).
The facility has ten (10) tanks (TANKCOND001-010) on site to store condensate and two (2) tanks
(TANKPW001-002) to store produced water prior to removal from the site. The flashing, working and
breathing losses from the tanks are routed to the enclosed combustor to control emissions. The
enclosed combustor that will be used to control emissions is designed to achieve a VOC destruction
efficiency of 98 percent.
Condensate and produced water are transported off site on an as needed basis via tanker truck. Truck
loading connections are in place to pump condensate (L001) and produced water (L002) from the
storage tanks into tanker trucks. Emissions from the loading operations are vented to the atmosphere.
Emissions from the facility’s emission sources were calculated using the extended analysis of the
condensate and produced water from Sweeney No. 2H, one of the wells in Forest pad. Gas analysis from
Sweeney No. 2H, one of the wells in Forest pad, is used for emission calculation. These extended
analyses are considered representative of the materials from Edna Monroe, being in the same Marcellus
rock formation.
Edna Monroe Pad calculation of potential to emit included all of the emission sources that belong to the
same industrial grouping, are located on contiguous or adjacent properties, and are under the control of
the same person. The nearest emission source that belongs to the same industrial grouping and under
the control of the same person but not located on contiguous or adjacent property is the Estlack Pad.
This is approximately 0.65 miles southwest of the facility.
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment C
Description of Fugitive Emissions
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015 C-1
Attachment C
Description of Fugitive Emissions
Edna Monroe Well Pad
Antero Resources Corporation
Tyler County, West Virginia
Sources of fugitive emissions include loading operations, haul road emissions, equipment leaks, and
pneumatic control valves. Fugitive emissions were calculated using AP-42 factors. Routine equipment
leaks are assumed to be occurring continuously throughout the year. Loading operations and haul road
emissions only occur when tanker trucks are onsite. The fugitives emissions summary is also located in
Attachment O.
Equipment Leaks
Equipment include valves, flanges, and connectors installed in various process equipment such as gas
production unit heaters, compressor, pipelines, and separators. Emissions are assumed to be occurring
throughout the year. Detailed calculations are shown on Table 4.
Pneumatic Control Valves
Pneumatic control valves are part of the gas production unit heaters. These are intermittent low bleed
valves and their emissions are assumed to be occurring throughout the year. Detailed calculations are
shown on Table 5.
Loading Operations
Loading emissions occur when condensate and produced water are transferred out of the well site via
tanker trucks. Fugitive emissions were estimated using AP-42 loading loss formula, L= 12.46*SPM/T,
and Bryan & Engineering (BR&E) software known as Promax. Detailed calculations are shown in Table 8.
Haul Road Emissions
Haul road emissions are emitted when tanker trucks or service vehicles enter the Facility. The Facility is
flat and unpaved. Detailed calculations are shown on Table 12.
lb/hr lb/hr ton/yr
Haul Road/Road Dust Emissions
Paved Haul Roads
n/a
Unpaved Haul Roads PM, PM10, PM2.5 1.3291 0.6645 4.1859 MB
VOCs 6.2848 6.2848 5.5080
toluene (108883) 0.0009 0.0009 0.0008
ethyl benzene (100414) 0.0010 0.0010 0.0009
hexane (110543) 0.0086 0.0086 0.0075
o,m,p-xylenes (95476,108383,106423) 0.0022 0.0022 0.0019
CO2 Equivalent
CO2 (124389), CH43.2288 3.2288 12.3613
benzene (71432) 0.0002 0.0002 0.0002
TAPs (benzene) 0.0002 0.0002 0.0002
Benzene (71432) 0.0103
Toluene (108883) 0.0788
Ethyl benzene (100414) 0.1384
Hexane (110543) 0.8741
o,m,p-xylenes (95476,108383,106423) 0.3209
CO2 Equivalent
CO2 (124389)), CH4354.4988
VOCs 16.5870
TAPs (benzene) 0.0103
toluene (108883) 0.00E+00 0.00E+00 0.00E+00
ethyl benzene (100414) 0.00E+00 0.00E+00 0.00E+00
hexane (110543) 0.0136 0.0136 0.0596
o,m,p-xylenes (95476,108383,106423) 0.00E+00 0.00E+00 0.00E+00
CO2 Equivalent
CO2 (124389)), CH49.0327 9.0327 39.5633
VOCs 0.1145 0.1145 0.5015
TAPs (benzene) 0.00E+00 0.00E+00 0.00E+00
2 Give rate with no control equipment operating. If emissions occur for less than 1 hr, then record emissions per batch in minutes (e.g. 5 lb VOC/20 minute batch).
3 Give rate with proposed control equipment operating. If emissions occur for less than 1 hr, then record emissions per batch in minutes (e.g. 5 lb VOC/20 minute batch).
4 Indicate method used to determine emission rate as follows: MB = material balance; ST = stack test (give date of test); EE = engineering estimate; O = other
(specify).
FUGITIVE EMISSIONS SUMMARYAll Regulated Pollutants
Chemical Name/CAS 1
Maximum Potential
Uncontrolled Emissions 2
Maximum Potential
Controlled Emissions 3
0.0103
Est.
Method
Used 4ton/yr
8.3718
5.5080
0.00E+00
MB
Loading/Unloading Operations
0.0008
0.0009
0.0075
0.0019
12.3613
0.0002
0.0002
MB
354.4988
16.5870
0.0103
Does not apply Does not apply
Attachment C/O: G70-A Emissions Summary SheetFugitive Emissions Data Summary Sheet
1 List all regulated air pollutants. Speciate VOCs, including all HAPs. Follow chemical name with Chemical Abstracts Service (CAS) number. LIST Acids, CO, CS2, VOCs, H2S, Inorganics,
Lead, Organics, O3, NO, NO2, SO2, SO3, all applicable Greenhouse Gases (including CO2 and methane), etc. DO NOT LIST H2, H2O, N2, O2, and Noble Gases.
Equipment Leaks (Components)
0.00E+00
0.00E+00
0.0596
0.00E+00
Equipment Leaks (PCVs)
MB
0.0788
0.1384
0.8741
0.3209
39.5633
0.5015
Source Category Pollutant
Number of
Source
Components (1)
Number of
Components
Monitored by
Frequency2
Average Time to Repair
(days) (3)
Estimated
Annual
Emission Rate
(lb/yr) (4)
light liquid VOC (6,7)
heavy liquid VOC8
Non-VOC9
Gas VOC 500
First attempt within 5 days
of detection and final repair
within 15 days
8,280.76
Light Liquid VOC 520
First attempt within 5 days
of detection and final repair
within 15 days
24,272.31
Heavy Liquid VOC -- --
Non-VOC -- --
Gas VOC See Valves
First attempt within 5 days
of detection and final repair
within 15 days
see Valves
Non VOC See Valves
First attempt within 5 days
of detection and final repair
within 15 days
see Valves
VOC
Non-VOC
VOC
Non-VOC
VOC
Non-VOC
VOC 130
First attempt within 5 days
of detection and final repair
within 15 days
186.59
Non-VOC
First attempt within 5 days
of detection and final repair
within 15 days
790.50
VOC 590
First attempt within 5 days
of detection and final repair
within 15 days
434.28
Non-VOC 1,839.82
Attachment C: Leak Source Data Sheet
Flanges
Other
Pumps (5)
Valves (10)
Safety Relief
Valves (11)
Open-ended
Lines (12)
Sampling Connections
(13)
Compressors
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment D
Process Flow Diagram
3-PHASE SEPARATORS WITH
HEATER (10)
*
H001
H002
H003
CONDENSATE TANKS (10)
TANKCOND001
TANKCOND002
TANKCOND003
TANKCOND004
PRODUCED WATER TANKS (2)
TANKPW001
TANKPW002
H004
WELL HEADS
SALES GAS
400 bbl
PRODUCED
WATER TANKS
(2)
400 bbl
CONDENSATE
TANKS
(10)
TRUCK LOADING
L001
PRODUCTS
COMBUSTION
PILOT GAS
TRUCK LOADING
L002
TRAFFIC
UNPAVED ROAD
HR001
CO
MB
US
TO
R
EC
001
PRODUCTS
COMBUSTION
(10)
M
METER
GAS
EMISSIONS
LOADING
EMISSIONS
LOADING
EMISSIONS
HAULING
*
*
WO
RK
IN
G/
FLA
SH
IN
G/
BR
EA
TH
IN
G
WO
RK
IN
G/
FLA
SH
IN
G/
BR
EA
TH
IN
G
EP-L001
EP-L002
EP-HR001
FUGITIVES
F001
EP-H001
EP-H002
EP-H003
EP-H004
GAS
COMPRESSOR
ENGINE
ENG001
EP-ENG001
PRODUCTS
COMBUSTION
TANKCOND006
TANKCOND007
TANKCOND008
TANKCOND009
TANKCOND005 TANKCOND010
H006
H007
H008
H009
EP-H006
EP-H007
EP-H008
EP-H009
H005 EP-H005 H010 EP-H010
EN
CLO
SE
D
CONDENSATE
GAS
FUEL
3-PHASE SEPARATORS
(10)
WITH HEATERS
*
EP-PCV
2-PHASE
(10)
SEPARATORS
GAS
LIQUID
PRODUCED
Attachment D
PROCESS FLOW DIAGRAM - ANTERO RESOURCES
EDNA MONROE WELL PAD
82715-00(197)GN-WA001 MAY 13/2015
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment E
Plot Plan
TANKCOND007TANKCOND008TANKCOND009TANKCOND010TANKPW001TANKPW002
L001L002
(EP-L001,EP-L002)
HAULING ROUTE(EP-HR001)
HR001
LEASEBURG UNIT 1HLEASEBURG UNIT 2HBEAD UNIT 1H
ACCESS ROAD
FACILITYFUGITIVES
F001
ENG001
COMPRESSORENGINE
(EP-ENG001)
PRODUCTIONEQUIPMENT
H001
(EP-PCV)
(EP-H001)H002H003
(EP-H002)(EP-H003)
H004 (EP-H004)
EC001
ENCLOSEDCOMBUSTOR
(EP-EC001)
H005 (EP-H005)
H006 (EP-H006)H007H008
(EP-H007)(EP-H008)
H009 (EP-H009)H010 (EP-H010)
TANKCOND006TANKCOND005TANKCOND004TANKCOND003TANKCOND002TANKCOND001BEAD UNIT 2H
DEULLEY UNIT 1HDEULLEY UNIT 3HDEULLEY UNIT 2HSECKMAN UNIT 3HSECKMAN UNIT 2HSECKMAN UNIT 1H
Attachment EPLOT PLAN
EDNA MONROE WELL PADANTERO RESOURCES
82715-00(197)GN-WA002 APR 27/2015
0 40 80ft 0
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment F
Area Map
1/2 Mile
Radius300 ft.
48
PROPERTY
RESIDENCE
RESIDENCE
Attachment FAREA MAP
EDNA MONROE WELL PADANTERO RESOURCES
82715-00(197)GN-WA003 APR 27/2015
SOURCE: USGS QUADRANGLE MAPS;MIDDLEBOURNE AND SHIRLEY, WEST VIRGINIA
0 2000ft1000
SITE COORDINATES: LAT. 39.422626, LONG. -80.873179SITE ELEVATION: 1063 ft AMSL
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment G
Emission Unit Data Sheets/G70-A Section Applicability Form
G70-A Oil and Natural Gas Production Facilities Instructions and Forms _____________________________________________________________________________________________
Page 15
General Permit G70-A Registration Section Applicability Form
General Permit G70-A was developed to allow qualified applicants to seek registration for a variety of sources. These sources include natural gas well affected facilities, storage tanks, natural gas-fired compressor engines (RICE), natural gas producing units, natural gas-fired in-line heaters, pneumatic controllers, heater treaters, tank truck loading, glycol dehydration units, completion combustion devices, flares, enclosed combustion devices, and vapor recovery systems. All registered facilities will be subject to Sections 1.0, 2.0, 3.0, and 4.0.
General Permit G70-A allows the registrant to choose which sections of the permit they are seeking registration under. Therefore, please mark which additional sections that you are applying for registration under. If the applicant is seeking registration under multiple sections, please select all that apply. Please keep in mind, that if this registration is approved, the issued registration will state which sections will apply to your affected facility. Section 5 Natural Gas Well Affected Facility Section 6 Storage Vessels* Section 7 Gas Producing Units, In-Line Heaters, Heater Treaters, and Glycol Dehydration Reboilers Section 8 Pneumatic Controllers Affected Facility (NSPS, Subpart OOOO) Section 9 Reserved Section 10 Natural gas-fired Compressor Engine(s) (RICE) ** Section 11 Tank Truck Loading Facility *** Section 12 Standards of Performance for Storage Vessel Affected Facilities (NSPS, Subpart OOOO) Section 13 Standards of Performance for Stationary Spark Ignition Internal Combustion Engines (NSPS, Subpart JJJJ) Section 14 Control Devices not subject to NSPS, Subpart OOOO Section 15 National Emissions Standards for Hazardous Air Pollutants for Stationary Reciprocating Internal Combustion Engines (40CFR63, Subpart ZZZZ) Section 16 Glycol Dehydration Units Section 17 Dehydration Units With Exemption from NESHAP Standard, Subpart HH § 63.764(d) (40CFR63, Subpart HH) Section 18 Dehydration Units Subject to NESHAP Standard, Subpart HH and Not Located Within an UA/UC (40CFR63, Subpart HH) Section 19 Dehydration Units Subject to NESHAP Standard, Subpart HH and Located Within an UA/UC (40CFR63, Subpart HH) * Applicants that are subject to Section 6 may also be subject to Section 12 if the applicant is subject to the NSPS,
Subpart OOOO control requirements or the applicable control device requirements of Section 14. ** Applicants that are subject to Section 10 may also be subject to the applicable RICE requirements of Section 13
and/or Section 15. *** Applicants that are subject to Section 11 may also be subject to control device requirements of Section 14.
✔
✔
✔
✔
✔
✔
✔
✔
G70-A Oil and Natural Gas Production Facilities
Instructions and Forms
_____________________________________________________________________________________________
Page 20
NATURAL GAS WELL AFFECTED FACILITY DATA SHEET
Complete this data sheet if you are the owner or operator of a gas well affected facility for which construction, modification,
or reconstruction commenced after August 23, 2011. This form must be completed for natural gas well affected facilities
regardless of when flowback operations occur (or have occurred).
Please provide the API number(s) for each NG well at this facility:
Note: This is the same API well number(s) provided in the well completion notification and as provided to the WVDEP,
Office of Oil and Gas for the well permit. The API number may be provided on the application without the state code (047).
Every oil and gas well permitted in West Virginia since 1929 has been issued an API (American Petroleum Institute) number.
This API is used by agencies to identify and track oil and gas wells.
The API number has the following format: 047-001-00001
Where,
047 = State code. The state code for WV is 047.
001 = County Code. County codes are odd numbers, beginning with 001 (Barbour) and continuing to 109 (Wyoming).
00001= Well number. Each well will have a unique well number.
10 wells unpermitted
Emission
Unit ID1
Emission
Point ID2
Emission Unit
Description
Year Installed/
Modified
Design
Capacity
Type3 and Date
of Change
Control
Device 4
H001, H002, H003,
H004, H005, H006,
H007, H008, H009,
H010
EP-H001, EP-H002,
EP-H003, EP-H004,
EP-H005, EP-H006,
EP-H007, EP-H008,
EP-H009, EP-H010
Gas Production Unit
Heater2016
1.5 MMBtu/hr
(each)New N/A
F001 F001 Fugitives 2016 New N/A
TANKCOND001-010 EP-EC001 Condensate Tanks 2016 400 bbl each New EP-EC001
TANKPW001-002 EP-EC001 PW Tanks 2016 400 bbl each New EP-EC001
L001 EP-L001 Loading (Condensate) 2016
200BBL
capacity
(each)
New N/A
L002 EP-L002 Loading (Water) 2016
200BBL
capacity
(each)
New N/A
HR001 EP-HR001 Haul Truck 201640 ton
capacityNew N/A
EC001 EP-EC001 Enclosed Combustor 2016 90 scf/min New N/A
PCV EP-PCV Pneumatic CV 20166.6
scf/day/PCVNew N/A
ENG001 EP-ENG001 Compressor Engine 2016 24HP New N/A
Attachment G: Emission Units Data Sheet (includes all emission units and air pollution control devices
that will be part of this permit application review, regardless of permitting status)
1 For Emission Units (or Sources) use the following numbering system:1S, 2S, 3S,... or other appropriate designation.
2 For Emission Points use the following numbering system:1E, 2E, 3E, ... or other appropriate designation.
3 New, modification, removal.
4 For Control Devices use the following numbering system: 1C, 2C, 3C,... or other appropriate designation.
Provide the following information for each new or modified bulk liquid storage tank.
I. GENERAL INFORMATION (required)
TANKCOND001-010
EP-EC001
II. TANK INFORMATION (required)
17,629,500 48,300
105 168
III. TANK CONSTRUCTION AND OPERATION INFORMATION (check which one applies)
Refer to enclosed TANKS Summary Sheets
X Refer to the responses to items 19 – 26 in section VII
IV. SITE INFORMATION (check which one applies)
Refer to enclosed TANKS Summary Sheets
X Refer to the responses to items 27 – 33 in section VII
V. LIQUID INFORMATION (check which one applies)
Refer to enclosed TANKS Summary Sheets
X Refer to the responses to items 34 – 39 in section VII
CONDTANK
TANKCOND001-010
5. Date Installed or Modified (for existing tanks): New 6. Type of change: NA
12. Nominal Capacity (specify barrels or gallons) . This is also known as “working volume." 400bbls
13A. Maximum annual throughput (gal/yr) 13B. Maximum daily throughput
(gal/day)
16. Tank fill method: Splash Fill
17. Is the tank system a variable vapor space system? No
If yes, (A) What is the volume expansion capacity of the system (gal)?
(B) What are the number of transfers into the system per year?
18. Type of tank (check all that apply):
X Fixed Roof X vertical horizontal X flat roof cone roof dome roof other (describe)
External Floating Roof pontoon roof double deck roof Domed External (or Covered) Floating Roof
Internal Floating Roof vertical column support self-supporting Variable Vapor Space lifter roof
diaphragm
Pressurized spherical cylindrical Underground
Other (describe)
14. Number of tank turnovers per year
Attachment G: Storage Vessel Emission Unit Data Sheet (Condensate)
1. Bulk Storage Area Name
3. Emission Unit ID number
2. Tank Name
4. Emission Point ID number
10A. Maximum Liquid Height (ft.) 18 10B. Average Liquid Height (ft.) 10
11A. Maximum Vapor Space Height (ft.) 18 11B. Average Vapor Space Height (ft.) 10
7A. Description of Tank Modification (if applicable) NA
7B. Will more than one material be stored in this tank? If so, a separate form must be completed for each material.
No
7C. Provide any limitations on source operation affecting emissions. (production variation, etc.)
8. Design Capacity (specify barrels or gallons). Use the internal cross-sectional area multiplied by internal height.
400bbls
9A. Tank Internal Diameter (ft.) 12 9B. Tank Internal Height (ft.) 20
15. Maximum tank fill rate (gal/min)
Provide the following information for each new or modified bulk liquid storage tank.
Attachment G: Storage Vessel Emission Unit Data Sheet (Condensate)
VI. EMISSIONS AND CONTROL DEVICE DATA (required)
lb/hr tpy
1 EPA = EPA Emission Factor, MB = Material Balance, SS = Similar Source, ST = Similar Source Test, Throughput Data, O = Other (specify)
Remember to attach emissions calculations, including TANKS Summary Sheets and other modeling summary sheets if applicable.
SECTION VII (required if did not provide TANKS Summary Sheets)
40. Emission Control Devices (check as many as apply):
Does Not Apply Rupture Disc (psig)
Carbon Adsorption1 Inert Gas Blanket of
X Vent to Vapor Combustion Device1 (vapor combustors, flares, thermal oxidizers) Condenser
1
Conservation Vent (psig
Other1 (describe) Vacuum Setting Pressure Setting Emergency Relief Valve (psig)
1 Complete appropriate Air Pollution Control Device Sheet
41. Expected Emission Rate (submit Test Data or Calculations here or elsewhere in the application).
Material Name and
CAS No.
Flashing Loss Breathing Loss Working Loss
lb/hr tpy tpy
Total Emissions
Loss
tpylb/hr lb/hr
Please see Tables 6 and 7
TANK CONSTRUCTION AND OPERATION INFORMATION
19. Tank Shell Construction: Steel
20A. Shell Color: Green 20B. Roof Color: Green 20C. Year Last Painted: 2016
21. Shell Condition (if metal and unlined): No Rust
25. Complete item 25 for Floating Roof Tanks Does not apply
25A. Year Internal Floaters Installed:
25B. Primary Seal Type (check one): Metallic (mechanical) shoe seal Liquid mounted resilient seal
25C. Is the Floating Roof equipped with a secondary seal? Yes No
25D. If yes, how is the secondary seal mounted? (check one) Shoe Rim Other (describe):
25E. Is the floating roof equipped with a weather shield? Yes No
22A. Is the tank heated? No 22B. If yes, operating temperature: 22C. If yes, how is heat provided to
tank?
23. Operating Pressure Range (psig): 0
24. Is the tank a Vertical Fixed Roof Tank? Yes 24A. If yes, for dome roof provide radius (ft): 24B. If yes, for cone roof, provide slop
(ft/ft):
25F. Describe deck fittings:
26. Complete the following section for Internal Floating Roof Tanks Does not apply
26A. Deck Type: Bolted Welded 26B. For bolted decks, provide deck construction:
26C. Deck seam. Continuous sheet construction:
26D. Deck seam length (ft.): 26E. Area of deck (ft2): 26F. For column supported 26G. For column supported
Provide the following information for each new or modified bulk liquid storage tank.
Attachment G: Storage Vessel Emission Unit Data Sheet (Condensate)
0.7429
0.9934
1.3075
51.7 39.5 63.8
36B. Corresponding vapor pressure
(psia):
37B. Corresponding vapor pressure
(psia):
38B. Corresponding vapor pressure
(psia):
32. Annual Avg. Solar Insulation Factor (BTU/ft2-day): 33. Atmospheric Pressure (psia): 14.8
LIQUID INFORMATION:
34. Avg. daily temperature range of bulk liquid
(°F):
34A. Minimum (°F): 34B. Maximum (°F):
SITE INFORMATION:
27. Provide the city and state on which the data in this section are based: Charleston, WV
28. Daily Avg. Ambient Temperature (°F): 55.3 29. Annual Avg. Maximum Temperature (°F): 75.94
30. Annual Avg. Minimum Temperature (°F): 65.9 31. Avg. Wind Speed (mph): 5.9
1030.235999
38A. Maximum liquid surface temperature (°F): 63.8
39. Provide the following for each liquid or gas to be stored in the tank. Add additional pages if necessary.
39A. Material name and composition: Condensate
35. Avg. operating pressure range of tank
(psig): 0
35A. Minimum (psig): 0 35B. Maximum (psig): 0
36A. Minimum liquid surface temperature (°F): 39.5
37A. Avg. liquid surface temperature (°F): 51.7
39D. Liquid molecular weight (lb/lb-mole): 97.4
39E. Vapor molecular weight (lb/lb-mole): 41.94
39B. CAS number: mix of HC
39C. Liquid density (lb/gal): 5.77
39H. Months Storage per year. From:
To:
year round
39F. Maximum true vapor pressure (psia): 1.5672
39G. Max Reid vapor pressure (psi): 2.65000
Provide the following information for each new or modified bulk liquid storage tank.
I. GENERAL INFORMATION (required)
TANKPW001-002
EP-EC001
II. TANK INFORMATION (required)
211,554,000 579,600
6297 168
III. TANK CONSTRUCTION AND OPERATION INFORMATION (check which one applies)
Refer to enclosed TANKS Summary Sheets
X Refer to the responses to items 19 – 26 in section VII
IV. SITE INFORMATION (check which one applies)
Refer to enclosed TANKS Summary Sheets
X Refer to the responses to items 27 – 33 in section VII
V. LIQUID INFORMATION (check which one applies)
Refer to enclosed TANKS Summary Sheets
X Refer to the responses to items 34 – 39 in section VII
14. Number of tank turnovers per year 15. Maximum tank fill rate (gal/min)
16. Tank fill method Splash Fill
17. Is the tank system a variable vapor space system? No
If yes, (A) What is the volume expansion capacity of the system (gal)?
(B) What are the number of transfers into the system per year?
18. Type of tank (check all that apply):
X Fixed Roof X vertical horizontal X flat roof cone roof dome roof other (describe)
External Floating Roof pontoon roof double deck roof Domed External (or Covered) Floating Roof
Internal Floating Roof vertical column support self-supporting Variable Vapor Space lifter roof
diaphragm
Pressurized spherical cylindrical Underground
Other (describe)
10A. Maximum Liquid Height (ft.) 18 10B. Average Liquid Height (ft.) 10
11A. Maximum Vapor Space Height (ft.) 18 11B. Average Vapor Space Height (ft.) 10
12. Nominal Capacity (specify barrels or gallons) . This is also known as “working volume." 400bbls
13A. Maximum annual throughput (gal/yr) 13B. Maximum daily throughput
(gal/day)
7A. Description of Tank Modification (if applicable) NA
7B. Will more than one material be stored in this tank? If so, a separate form must be completed for each material.
No
7C. Provide any limitations on source operation affecting emissions. (production variation, etc.)
8. Design Capacity (specify barrels or gallons). Use the internal cross-sectional area multiplied by internal height.
400bbls
9A. Tank Internal Diameter (ft.) 12 9B. Tank Internal Height (ft.) 20
Attachment G: Storage Vessel Emission Unit Data Sheet (Produced Water)
1. Bulk Storage Area Name 2. Tank Name
3. Emission Unit ID number 4. Emission Point ID number
5. Date Installed or Modified (for existing tanks): New 6. Type of change: NA
PWTANK
TANKPW001-002
Provide the following information for each new or modified bulk liquid storage tank.
Attachment G: Storage Vessel Emission Unit Data Sheet (Produced Water)
VI. EMISSIONS AND CONTROL DEVICE DATA (required)
lb/hr tpy
1 EPA = EPA Emission Factor, MB = Material Balance, SS = Similar Source, ST = Similar Source Test, Throughput Data, O = Other (specify)
Remember to attach emissions calculations, including TANKS Summary Sheets and other modeling summary sheets if applicable.
SECTION VII (required if did not provide TANKS Summary Sheets)
25F. Describe deck fittings:
26. Complete the following section for Internal Floating Roof Tanks Does not apply
26A. Deck Type: Bolted Welded 26B. For bolted decks, provide deck construction:
26C. Deck seam. Continuous sheet construction:
26D. Deck seam length (ft.): 26E. Area of deck (ft2): 26F. For column supported 26G. For column supported
25. Complete item 25 for Floating Roof Tanks Does not apply
25A. Year Internal Floaters Installed:
25B. Primary Seal Type (check one): Metallic (mechanical) shoe seal Liquid mounted resilient seal
25C. Is the Floating Roof equipped with a secondary seal? Yes No
25D. If yes, how is the secondary seal mounted? (check one) Shoe Rim Other (describe):
25E. Is the floating roof equipped with a weather shield? Yes No
22A. Is the tank heated? No 22B. If yes, operating temperature: 22C. If yes, how is heat provided to
tank?
23. Operating Pressure Range (psig): 0
24. Is the tank a Vertical Fixed Roof Tank? Yes 24A. If yes, for dome roof provide radius (ft): 24B. If yes, for cone roof, provide slop
(ft/ft):
TANK CONSTRUCTION AND OPERATION INFORMATION
19. Tank Shell Construction: Steel
20A. Shell Color: Green 20B. Roof Color: Green 20C. Year Last Painted: 2016
21. Shell Condition (if metal and unlined): No Rust
Please see Tables 6 and 7
41. Expected Emission Rate (submit Test Data or Calculations here or elsewhere in the application).
Material Name and
CAS No.
Flashing Loss Breathing Loss Working Loss Total Emissions
Loss
lb/hr tpy tpy lb/hr lb/hr tpy
40. Emission Control Devices (check as many as apply):
Does Not Apply Rupture Disc (psig)
Carbon Adsorption1 Inert Gas Blanket of
X Vent to Vapor Combustion Device1 (vapor combustors, flares, thermal oxidizers) Condenser1
Conservation Vent (psig
Other1 (describe) Vacuum Setting Pressure Setting Emergency Relief Valve (psig)
1 Complete appropriate Air Pollution Control Device Sheet
Provide the following information for each new or modified bulk liquid storage tank.
Attachment G: Storage Vessel Emission Unit Data Sheet (Produced Water)
0.1837
0.2596
0.3600
39G. Max Reid vapor pressure (psi): 1.02325
39H. Months Storage per year. From:
To:
year round
39E. Vapor molecular weight (lb/lb-mole): 18.3250
39F. Maximum true vapor pressure (psia): 0.4467
39C. Liquid density (lb/gal): 8.33
39D. Liquid molecular weight (lb/lb-mole): 18.0156
39. Provide the following for each liquid or gas to be stored in the tank. Add additional pages if necessary.
39A. Material name and composition: Produced Water
39B. CAS number: mix of HC and water
36A. Minimum liquid surface temperature (°F): 39.5 36B. Corresponding vapor pressure
(psia):
37A. Avg. liquid surface temperature (°F): 51.7 37B. Corresponding vapor pressure
(psia):
38A. Maximum liquid surface temperature (°F): 63.8 38B. Corresponding vapor pressure
(psia):
51.7 39.5 63.8
35. Avg. operating pressure range of tank
(psig): 0
35A. Minimum (psig): 0 35B. Maximum (psig): 0
32. Annual Avg. Solar Insulation Factor (BTU/ft2-day): 33. Atmospheric Pressure (psia): 14.8
1030.235999
LIQUID INFORMATION:
34. Avg. daily temperature range of bulk liquid
(°F):
34A. Minimum (°F): 34B. Maximum (°F):
SITE INFORMATION:
27. Provide the city and state on which the data in this section are based: Charleston, WV
28. Daily Avg. Ambient Temperature (°F): 55.3 29. Annual Avg. Maximum Temperature (°F): 75.94
30. Annual Avg. Minimum Temperature (°F): 65.9 31. Avg. Wind Speed (mph): 5.9
Emission
Unit ID #1
Emission
Point ID#2
Emission Unit Description
(Manufacturer / Model #)
Year
Installed/
Modified
Type3 and
Date of
Change
Control
Device4
Design Heat
Input
(mmBtu/hr)5
Fuel Heating
Value
(Btu/scf)6
H001 EP-H001 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H002 EP-H002 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H003 EP-H003 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H004 EP-H004 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H005 EP-H005 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H006 EP-H006 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H007 EP-H007 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H008 EP-H008 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H009 EP-H009 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
H010 EP-H010 Gas Production Unit Heater 2016 New -- 1.50 1,247.06
ENG001 EP-ENG001 Engine (Kubota DG972-E2) 2016 New -- -- 1,247.06
EC001 EP-EC001Enclosed Combustor
(Cimarron)2016 New EP-EC001 6.6 1,247.06
3 New, modification, removal.
4 Complete appropriate air pollution control device sheet for any control device.
5 Enter design heat input capacity in mmBtu/hr.
6 Enter the fuel heating value in Btu/standard cubic foot.
Attachment G: Natural Gas Fired Fuel Burning Units
Emission Data Sheet
Complete the information on this data for each Gas Producing Unit(s), Heater Treater(s), and in-line heater(s) at the
production pad. Reboiler information should be entered on the Glycol Dehydration Emission Unit Data Sheet.
2 Enter the appropriate Emission Point identification numbers for each fuel burning unit located at the production pad. Gas Producing Unit Burners should be designated GPU-
1, GPU-2, etc. Heater Treaters should be designated HT-1, HT-2, etc. Heaters or Line Heaters should be designated LH-1, LH-2, etc. For emission points, use 1E, 2E, 3E…or other
appropriate designation.
1 Enter the appropriate Emission Unit (or Sources) identification numbers for each fuel burning unit located at the production pad. Gas Producing Unit Burners should be
designated GPU-1, GPU-2, etc. Heater Treaters should be designated HT-1, HT-2, etc. Heaters or Line Heaters should be designated LH-1, LH-2, etc. For sources, use 1S, 2S,
3S…or other appropriate designation. Enter glycol dehydration unit Reboiler Vent data on the Glycol Dehydration Unit Data Sheet.
Complete this section for any natural gas-fired reciprocating internal combustion engine.
Reference lbs/hr tons/yr
MD 0.3158 1.3831
MD 5.6445 24.7228
AP 0.0071 0.0311
AP 0.0001 0.0006
AP 0.0024 0.0104
AP 0.0049 0.0215
Emission Point ID No. EP-ENG001
Attachment G: Natural Gas-Fired Compressor Engine (RICE)
Emission Unit Data Sheet
Emission Unit (Source) ID No. ENG001
Engine Manufacturer and Model Engine (Kubota DG972-E2)
Manufacturer’s Rated bhp/rpm 24 HP @ 3600 rpm
Source Status NS
Date Installed/Modified/Removed January 2016
Engine Manufactured/Reconstruction Date 2013
Is this engine subject to 40CFR60, Subpart JJJJ? Yes
Is this a Certified Stationary Spark Ignition Engine according
to 40CFR60, Subpart JJJJ? (Yes or No)Yes
Is this engine subject to 40CFR63, Subpart ZZZZ? (yes or no) Yes
Fuel throughput (MMft3/yr) 1.6907
APCD Type -
Fuel Type
Operating bhp/rpm 16.5 HP @ 2400 rpm
BSFC (Btu/bhp-hr)
RG
H2S (gr/100 scf) 0
NOX
CO
VOC
Fuel throughput (ft3/hr) 193
MRR
Proposed Monitoring:
Proposed Reporting:
Engine, Fuel and
Combustion Data
Engine Type RB4S
SO2
PM10
Operation (hrs/yr) 8760
9773
Potential Emissions
Formaldehyde
N/A
Proposed Recordkeeping:
1) Maintain records of
maintenance performed
on engines.
2) Documentation from
manufacturer that engine
is certified to meet
emission standards
Monitor engine setting
adjustments to ensure
these are consistent with
manufacturer's
instructions.
Furnish the following information for each new or modified bulk liquid transfer area or loading rack at the natural gas production pad.
This form is to be used for bulk liquid transfer operations to tank trucks.
2016
Oct. - Dec.
16
7
2 At maximum bulk liquid temperature
3 B = Ballasted Vessel, C = Cleaned, U = Uncleaned (dedicated service), O = other (describe)
4 List as many as apply (complete and submit appropriate Air Pollution Control Device Sheets as Attachment “H” ):
CA = Carbon Adsorption
VB = Dedicated Vapor Balance (closed system) ECD = Enclosed Combustion Device
F = Flare
TO = Thermal Oxidation or Incineration
5 EPA = EPA Emission Factor as stated in AP-42
10. Proposed Monitoring, Recordkeeping, Reporting, and Testing
MONITORING
1) Visual inspection to ensure that loading connections
from storage tanks to trucks are leak-free.
RECORDKEEPING
1) Maintain records of condensate transferred from storage
tanks.
2) Maintain records of produced water transferred from
storage tanks.
REPORTING
N/A
TESTING
N/A
11. Describe all operating ranges and maintenance procedures required by Manufacturer to maintain warranty: N/A
Estimation Method 5 Promax Promax
Notes:
1 BF = Bottom Fill SP = Splash Fill SUB = Submerged Fill
Maximum
Emission Rate
Loading (lb/hr) 9.31 1.16
Annual (ton/yr) 8.15 12.17
Minimum collection efficiency (%) 0 0
Minimum control efficiency (%) 0 0
Cargo Vessel Condition3
U U
Control Equipment or Method 4
None None
Max. Bulk Liquid Temperature (oF) 72.1 72.1
True Vapor Pressure 2
1.57 0.45
Max. Fill Rate (gal/min) 168 168
Average Fill Time (min/loading) 50 50
Max. annual throughput (1000 gal/yr) 17,629.50 211,554.00
Loading Method 1 BF BF
9. Bulk Liquid Data (add pages as necessary)
Liquid Name Condensate Produced Water
Max. daily throughput (1000 gal/day) 48.3 579.6
Attachment G: Tank Truck Loading
Emissions Unit Data Sheet
Jan. - Mar.
16
7
Apr. - June
16
5A. Number of pumps: 4 5B. Number of liquids loaded: 2 5C. Maximum number of
tank trucks loading at one time: 4
6. Describe cleaning location, compounds and procedure for tank trucks: For hire tank trucks are used and are cleaned
at the operator's dispatch terminal. These trucks are in dedicated service and cleaned only prior to repair or leak tests.
Cleaning materials include water, steam, detergent, and solvents which are applied using hand held pressurized spray
nozzles.
4. Emission Unit Description: CONDENSATE AND PRODUCED WATER
5. Loading Area Data
8. Projected Maximum Operating Schedule (for rack or transfer point as a whole):
Maximum
days/week
1. Emission Unit ID: L001, L002 2. Emission Point
ID:
3. Year
Installed/
Modified:
EP-L001, EP-L002
7
July - Sept.
16
7
7. Are tank trucks pressure tested for leaks at this or any other location?
X Yes No
If YES, describe: Tank trucks are pressure tested for leaks at the location of the leak testing company. Trucks are tested
using EPA Method 27-internal vapor valve test and issued certification that DOT requirements are met.
hours/day
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment H
Air Pollution Control Device Data Sheet
scfd
20. Type/Grade of
pilot fuel:
Natural Gas
Attachment H: Air Pollution Control Device
Vapor Combustion Control Device Sheet
1. Control Device ID#: EC001
8. Hours of operation per year: 8760
Complete this vapor combustion control device sheet for each enclosed combustion device, flare, thermal oxidizer, or completion combustion
device that is located at the natural gas production pad for the purpose of thermally destructing waste gas to control emissions of regulated
pollutants to the atmosphere.
F/W/B Emissions from TANKCOND 98 98
F/W/B Emissions from TANKPW 98 98
29. Pollutant(s) Controlled 30. % Capture Efficiency 31. Manufacturer’s Guaranteed Control
Efficiency (%)
21. Number of pilot lights: 22. Fuel flow rate to
pilot flame per pilot
(scf/hr):
23. Heat input per pilot
(BTU/hr):
24. Will automatic re-
ignition be used?
1 12.6 12800 Yes
25. If automatic re-ignition will be used, describe the method: Based on a monitoring system
26. Describe the method of controlling flame: Flame Rectification, a thermocouple equivalent
27. Is pilot flame equipped with a monitor
to detect the presence of the flame?
Yes
28. If yes, what type? Thermocouple
If this vapor combustor controls emissions from more than six emission units, please attach additional pages.
Pilot Information
Steam - Air - Pressure - X Non - 25 3.33 Yes
Waste Gas Information
15. Maximum waste gas flow
rate (scfm):
16. Heat value of waste gas
stream (BTU/ft3)
17. Temperature of the
emissions stream (°F)
18. Exit Velocity of the
emissions stream (ft/s)
87.78 1,792.39 900 1.68E-01
19. Provide an attachment with the characteristics of the waste gas stream to be burned.
11. Assist Type 12. Flare Height
(ft)
13. Tip Diameter (ft) 14. Was the design per
§60.18?
TANKCOND001-010 Condensate Tank
TANKPW001-002 PW Tanks
Control Device Information
6. Select the type of vapor combustion control device being used: Enclosed Combustor
7. Manufacturer: Model No. Cimarron Model No. 48" HV ECD
9. List the emission units whose emissions are controlled by this vapor combustion control device: (Emission Point ID#:)
10. Emission Unit ID# Emission Source Description: Emission Unit ID# Emission Source Description:
IMPORTANT: READ THE INSTRUCTIONS ACCOMPANYING THIS FORM BEFORE COMPLETING.
General Information
2. Installation Date: New
3. Maximum Rated Total Flow Capacity: 4. Maximum Design Heat Input: 5. Design Heat Content:
131,000 6.6 MMBtu/hr 2300 BTU/scf
Attachment H: Air Pollution Control Device
Vapor Combustion Control Device SheetComplete this vapor combustion control device sheet for each enclosed combustion device, flare, thermal oxidizer, or completion combustion
device that is located at the natural gas production pad for the purpose of thermally destructing waste gas to control emissions of regulated
pollutants to the atmosphere.
If any of the requested information is not available, please contact the manufacturer.
32. Has the control device been tested by the manufacturer and certified? Yes, see spec sheet.
33. Describe all operating ranges and maintenance procedures required by the manufacturer to maintain warranty: See spec
sheet for operating ranges.
MONITORING
1) Report any period when visible emissions exceeded 5 minutes during any two-hour period.
2) Monitor the presence of pilot flame at all times with the Flame rectification system, a thermocouple equivalent.
3) Monitor visible emissions from the vapor combustor.
4) Monitor throughput to the vapor combustor.
RECORDKEEPING
1) Record the times and duration of periods when the pilot flame was not present.
2) Records of throughput to the vapor combustor.
3) Records of vapor combustor malfunction or shutdown which resulted in excess emissions.
4) Records of vapor combustor inspection and maintenance activities conducted.
REPORTING
1) Report any period when visible emissions exceeded 5 minutes during any two-hour period.
34. Additional Information Attached? YES
Please attach a copy of manufacturer’s data sheet. Please attach a copy of manufacturer’s drawing.
Please attach a copy of the manufacturer’s performance testing.
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment I
Emission Calculations
Company NameAntero Resources
Corporation
Facility/Well Name Edna Monroe Well Pad
Nearest City/Town Middlebourne
API Number/SIC Code 1311
Latitude/Longitude 39.422626, -80.873179
County Tyler County
Max Condensate Site Throughput (bbl/day): 1,150
Max Produced Water Site Throughput (bbl/day): 13,800
Are there any sour gas streams at this site? No
Is this site currently operational/producing? No
Equipment/Process Types How many for this site?
Fugitives 10
IC Engines 1
Turbines 0
Diesel Engines 0
Gas Production Unit Heaters 10
Condensate Tanks 10
Produced Water Tanks 2
Miscellaneous Tanks 0
Loading Jobs 2
Glycol Units 0
Amine Units 0
Enclosed Combustors-Vapor Combustors 1
Equipment/Processes at Site
Table 1
Facility Information
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
Technical Information
Oil and Gas Site General Information
Administrative Information
CRA 082715 (197)
(lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr) (lbs/hr) (ton/yr)
UNCONTROLLED (Fugitives, Storage Tanks, Gas Production Unit Heaters)
Fugitive Emissions (Component Count, PCV and Hauling)1
3.9015 17.0884 89.969 394.06 0.5981 3.7673 0.3384 1.4821 0.0023 0.0103 7.33E-02 3.21E-01
Flashing, Working and Breathing (F/W/B) Losses2
280.21 1,227.3 1,761.4 7,715.1 7.001 30.666 0.2081 0.9114 0.4858 2.1276
Engine Emissions3
0.0071 0.0311 0.3158 1.3831 27.78 121.66 5.6445 24.7228 0.0001 0.0006 0.0024 0.0104 0.0023 0.0100 0.0055 0.0241 0.0004 0.0017 0.0000 0.0002 0.0049 0.0215
Gas Production Unit Heater Emissions4
0.0662 0.2898 1.2028 5.2684 1,451.97 6,359.64 1.0104 4.4254 0.0072 0.0316 0.0914 0.4004 0.0914 0.4004 6.01E-06 2.63E-05 2.26E-02 9.92E-02 2.53E-05 1.11E-04 0.0009 0.0040
TOTALS: 284.1815 1244.7148 1.5186 6.6515 3331.1620 14590.4895 6.6549 29.1482 0.0074 0.0322 0.0938 0.4108 0.6918 4.1777 6.01E-06 2.63E-05 7.3680 32.2717 0.2108 0.9235 0.5591 2.4487 0.0058 0.0255
UNCONTROLLED (Truck Loading Emissions)
Truck Loading Emissions5
6.285 5.508 3.229 12.361 0.0129 0.0113 1.98E-04 1.83E-04 0.0022 0.0019
CONTROLLED EMISSIONS
Enclosed Combustor Emissions (from F/W/B losses)6
5.6042 24.5464 0.5279 2.3124 2679.5754 11736.5401 0.4435 1.9424 7.56E-06 3.31E-05 0.0301 0.1318 0.0401 0.1757 2.64E-06 1.16E-05 0.1401 0.6134 4.16E-03 1.82E-02 0.0097 0.0426 9.45E-07 4.14E-06
Controlled Fugitive Emissions from Hauling 0.2990 1.8837
TOTALS: 5.6042 24.5464 0.5279 2.3124 2679.5754 11736.5401 0.4435 1.9424 7.56E-06 3.31E-05 0.0301 0.1318 0.3392 2.0594 2.64E-06 1.16E-05 0.1401 0.6134 0.0042 0.0182 0.0097 0.0426 9.45E-07 4.14E-06
POTENTIAL TO EMIT7
9.5789 47.4637 2.0465 8.9639 4249.2926 18624.2631 7.0983 31.0906 0.0074 0.0323 0.1239 0.5426 0.4329 2.4698 8.65E-06 3.79E-05 0.5066 2.2301 0.0069 0.0305 0.0830 0.3655 0.0058 0.0255
1 - See Tables 4 and 5 for fugitive emission calculations; Table 12 for PM emissions from hauling.
2 - See Tables 6 and 7 for tanks emission calculations.
3 - See Table 13 for engine emissions.
4 - See Table 9 for gas production unit heater emission calculations.
6 - See Table 10 and 11 for enclosed combustor emission calculations.
Table 2
Uncontrolled/Controlled Emissions Summary
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
XylenesPM10 Lead Total HAPs Benzene Formaldehyde
Enter any notes here:
SO2 PM2.5
Emission Source
VOC NOX CO2e CO
5 - The maximum emission was calculated based on tank truck capacity of 200 barrels and actual fill rate of 50 minutes per tank truck. At a production rate of 1150 barrels per day, VOC emissions would be 6.2848 pounds per hour when there is truck loading activity. Average
hourly VOC emissions from truck loading per year is 1.2575 pound per hour.
7 - The hourly potential to emit is the sum of emissions from gas production unit heaters, engine, storage tanks, fugitives and flare. Does not include emissions from loading (see footnote 5). The total TPY PTE is the sum of all emissions.
PM 10 TPY is the sum of uncontrolled hauling and other PM10 sources.
CRA 082715 (197)
Uncontrolled Controlled Threshold Uncontrolled Controlled
lbs/hr 284.1815 9.5789 6 Yes Yes
tons/yr 1250.2228 47.4637 10 Yes Yes
lbs/hr 1.5186 2.0465 6
tons/yr 6.6515 8.9639 10
lbs/hr 6.6549 7.0983 6 Yes Yes
tons/yr 29.1482 31.0906 10 Yes Yes
lbs/hr 0.0074 0.0074 6
tons/yr 0.0322 0.0323 10
lbs/hr 9.38E-02 1.24E-01 6
tons/yr 4.11E-01 5.43E-01 10
lbs/hr 0.6918 0.4329 6
tons/yr 4.1777 2.4698 10
lbs/hr 6.01E-06 8.65E-06 6
tons/yr 2.63E-05 3.79E-05 10
lbs/hr 7.3680 0.5066 2 Yes
tons/yr 32.2830 2.2301 5 Yes
Total TAPs lbs/hr 0.2167 0.0127 1.14
lbs/hr 5.8168 0.3465
tons/yr 25.4850 1.5252
lbs/hr 0.4753 0.0273
tons/yr 2.0826 0.1204
lbs/hr 0.3001 0.0370
tons/yr 1.3155 0.1628
lbs/hr 0.5591 0.0830
tons/yr 2.4506 0.3655
lbs/hr 0.2108 0.0069
tons/yr 0.9236 0.0305
1. Emissions are based on 98% Enclosed combustor DRE operating 100% of the time.
PM10
Lead
Total HAPs
Enter any notes
here:
PM2.5
n-Hexane
Toluene
Ethylbenzene
Xylenes
Benzene
Pollutant
VOC
NOX
CO
SO2
Emissions Threshold Exceeded?
Antero Resources Corporation
Table 3
Permit Summary
Edna Monroe Well Pad
Tyler County, West Virginia
2. Please see Attachment C/O- Fugitive Emissions Data Summary Sheet and
Attachment O – Emission Points Data Summary Sheet for sitewide sources
and breakdown of emission quantities.
CRA 082715 (197)
VOC Type:
Emission Type:
VOC frac 0.191
Benzene frac 0.000
Toluene 0.000
Ethylbenzene 0.000
Xylenes 0.000
n-Hexane 0.023
Methane 0.603
Number Component Pollutant
Emission Factor
(kg/hr of THC per
component)
kg/hr lb/yr
500 Valves Gas VOC 0.004500 0.43 8,280.76
Non VOC 0.004500 1.82 35,081.24
590 Connectors VOC 0.000200 0.02 434.28
Non-VOC 0.000200 0.10 1,839.82
130 Flanges VOC 0.000390 0.01 186.59
Non-VOC 0.000390 0.04 790.50
0.46 8,901.63
2.42 46,613.19
VOC frac 0.969
Benzene frac 0.001
Toluene 0.006
Ethylbenzene 0.011
Xylenes 0.026
n-hexane 0.028
Methane 0.011
Number Component Pollutant
Emission Factor
(kg/hr of THC per
component)
kg/hr lb/yr
520 Valves Light Liquid VOC 0.002500 1.26 24,272.31
Light Liquid Non-VOC 0.04 781.29
1.26 24,272.31
1.30 25,053.60
Annual Emissions
(lb/yr)Annual Emissions (lb/hr)
Annual Emissions
(tpy)
VOC 33,173.94 3.79 16.59
Ethylbenzene 0.03 0.14
Toluene 0.02 0.08
Xylenes 0.07 0.32
n-Hexane 0.20 0.87
TAPs (Benzene) 0.00 0.01
HAPs 0.32 1.42
CO2e 708,997.62 80.94 354.50
Fugitive emissions based on an estimated component count
Global Warming Potentials from EPA site
Reference to Emission factors used:
1. Emission factors are for oil and gas production facilities (not refineries) come from
the EPA's "Protocol for Equipment Leak Emission Estimates"
November 1995, EPA 4531, R-95-017, Table 2-4.
Antero Resources Corporation
Table 4
Fugitive Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Fugitive Total Emissions
Condensate VOC
Steady State (continuous)
Gas Weight Fraction From Analysis:
Gas
Total VOCs:
Total THC:
Enter Notes Here:
Light Liquid Weight Fraction From Analysis:
Light Liquid
Total VOC:
Total THC:
2. Percent of speciated VOCs used in fugitive calculations are based on the total hydrocarbons, not of
the total sample.
CRA 082715 (197)
Number of PCVs 40
Bleed Rate (scf/day/PCV) 6.6
Total Bleed Rate (scf/day) 264
Component Mol% Molecular Weight Component Flow Component Moles
(lb/lb-mole) (scf/day) (lb-moles) (lbs/day) (lbs/hr) (tons/year)
H2S 0 34.08 0 0.00 0.00 0.00 0.00
Nitrogen 0.4946 14.01 1.305744 0.00 0.05 0.00 0.01
Carbon Dioxide 0.1467 44.01 0.387288 0.00 0.04 0.00 0.01
Methane 77.6927 16.04 205.108728 0.54 8.67 0.36 1.58
Ethane 14.1987 30.07 37.484568 0.10 2.97 0.12 0.54
Propane 4.4938 44.1 11.863632 0.03 1.38 0.06 0.25
Isobutane 0.5666 58.12 1.495824 0.00 0.23 0.01 0.04
n-Butane 1.1838 58.12 3.125232 0.01 0.48 0.02 0.09
Isopentane 0.3749 72.15 0.989736 0.00 0.19 0.01 0.03
n-Pentane 0.2914 72.15 0.769296 0.00 0.15 0.01 0.03
2-Methylpentane 0 86.18 0 0.00 0.00 0.00 0.00
3-Methylpentane 0 86.18 0 0.00 0.00 0.00 0.00
n-Hexane 0.5451 86.18 1.439064 0.00 0.33 0.01 0.06
Methylcyclopentane 0 84.16 0 0.00 0.00 0.00 0.00
Benzene 0 78.11 0 0.00 0.00 0.00 0.00
2-Methylhexane 0 100.2 0 0.00 0.00 0.00 0.00
3-Methylhexane 0 100.2 0 0.00 0.00 0.00 0.00
Heptane 0 100.21 0 0.00 0.00 0.00 0.00
Methylcyclohexane 0 98.186 0 0.00 0.00 0.00 0.00
Toluene 0 92.14 0 0.00 0.00 0.00 0.00
Octane 0 114.23 0 0.00 0.00 0.00 0.00
Ethylbenzene 0 106.17 0 0.00 0.00 0.00 0.00
m & p-Xylene 0 106.16 0 0.00 0.00 0.00 0.00
o-Xylene 0 106.16 0 0.00 0.00 0.00 0.00
Nonane 0 128.2 0 0.00 0.00 0.00 0.00
C10+ 0 174.28 0 0.00 0.00 0.00 0.00
lb/hr tpy
VOC Emissions 0.1145 0.5015
Benzene Emissions 0.0000 0.0000
Toluene Emissions 0.0000 0.0000
Ethylbenzene Emissions 0.0000 0.0000
Xylene Emissions 0.0000 0.0000
n-Hexane Emissions 0.0136 0.0596
HAPs Emissions 0.0136 0.0596
TAPs Emissions 0.0000 0.0000
CO2e emissions 9.0327 39.5633
Enter any notes here:
1. PCV bleed rate obtained from the user manual for PCV
http://issuu.com/rmcprocesscontrols/docs/mizer-pilot-operation--parts---installation-manual
2. Emissions per hour= Mol % x no. of PCV x bleed rate x MW / 379.48 / 24
Table 5
Pneumatic Control Valve Emissions
Component Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
CRA 082715 (197)
# Hours Operational 8760
Vapor Mass Fraction Vapor Mass Fraction
wt% lbs/hr tpy wt% lbs/hr tpy
Water 0.0995 0.3603 1.5782 2.7258 0.0000 0.0000
H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Nitrogen 0.0061 0.0223 0.0975 0.3893 0.3427 1.5011
Carbon Dioxide 0.1298 0.4700 2.0587 2.0777 1.8290 8.0109
Methane 4.4478 16.1015 70.5245 61.3719 54.0258 236.6332
Ethane 25.1005 90.8670 397.9975 21.2881 18.7400 82.0811
Propane 30.7698 111.3906 487.8908 8.4858 7.4700 32.7188
Isobutane 7.4451 26.9522 118.0504 0.4697 0.4135 1.8109
n-Butane 13.9455 50.4844 221.1218 1.6811 1.4799 6.4819
Isopentane 5.1452 18.6263 81.5834 0.3736 0.3289 1.4405
n-Pentane 4.1372 14.9771 65.5995 0.2862 0.2520 1.1036
2-Methylpentane 1.8226 6.5979 28.8987 0.0570 0.0502 0.2198
3-Methylpentane 0.8846 3.2025 14.0270 0.0737 0.0649 0.2843
n-Hexane 1.5270 5.5278 24.2117 0.0377 0.0332 0.1455
Methylcyclopentane 0.3096 1.1207 4.9086 0.0751 0.0661 0.2895
Benzene 0.0414 0.1499 0.6566 0.0655 0.0577 0.2527
2-Methylhexane 0.6707 2.4281 10.6350 0.0184 0.0162 0.0711
3-Methylhexane 0.5226 1.8917 8.2857 0.0150 0.0132 0.0578
Heptane 0.9976 3.6115 15.8186 0.0300 0.0264 0.1157
Methylcyclohexane 0.5784 2.0937 9.1704 0.0922 0.0811 0.3553
Toluene 0.0922 0.3339 1.4627 0.1374 0.1209 0.5297
Octane 0.8869 3.2108 14.0631 0.0158 0.0139 0.0611
Ethylbenzene 0.0541 0.1960 0.8585 0.0795 0.0700 0.3067
m & p-Xylene 0.0324 0.1172 0.5134 0.0471 0.0415 0.1817
o-Xylene 0.0650 0.2355 1.0313 0.0980 0.0863 0.3780
Nonane 0.2258 0.8176 3.5809 0.0062 0.0055 0.0240
C10+ 0.0624 0.2260 0.9900 0.0019 0.0017 0.0075
Total VOCs 70.216 254.19 1,113.4 12.147 10.6932 46.8362
Total CO2e 403.01 1,765.2 1,352.47 5,923.8
Total TAPs (Benzene) 0.1499 0.6566 0.0577 0.2527
Toluene 0.3339 1.4627 0.1209 0.5297
Ethylbenzene 0.1960 0.8585 0.0700 0.3067
Xylenes 0.3527 1.5448 0.1278 0.5597
n-Hexane 5.528 24.212 0.0332 0.1455
Total HAPs 6.560 28.734 0.4096 1.7942
Total 100.00 362.01 1,585.6 100.00 85.631 375.06
Enter any notes here: Vapor mass fractions and Flashing losses from Promax output
Flashing Losses Flashing Losses
Condensate Tank Flashing Losses Produced Water Tank Flashing Losses
Table 6
Uncontrolled Flashing Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
CRA 082715 (197)
Condensate Tank Information
Number of Tanks 10
Maximum Working Losses (lbs/hr) 10.5760
Maximum Breathing Losses (lbs/hr) 12.1351
Vapor Mass Fraction
wt% lbs/hr tpy lbs/hr tpy lbs/hr tpy
H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Nitrogen 0.0002 0.0000 0.0001 0.0000 0.0001 0.0001 0.0002
Carbon Dioxide 0.1372 0.0145 0.0636 0.0167 0.0730 0.0312 0.1365
Methane 0.9553 0.1010 0.4425 0.1159 0.5078 0.2170 0.9503
Ethane 31.4443 3.3256 14.5659 3.8158 16.7132 7.1414 31.2791
Propane 32.7228 3.4608 15.1582 3.9709 17.3927 7.4317 32.5509
Isobutane 7.3520 0.7776 3.4057 0.8922 3.9077 1.6697 7.3134
n-Butane 13.5387 1.4319 6.2715 1.6429 7.1960 3.0748 13.4676
Isopentane 4.7333 0.5006 2.1926 0.5744 2.5158 1.0750 4.7085
n-Pentane 3.7605 0.3977 1.7420 0.4563 1.9988 0.8541 3.7408
2-Methylpentane 1.6221 0.1716 0.7514 0.1968 0.8622 0.3684 1.6136
3-Methylpentane 0.7852 0.0830 0.3637 0.0953 0.4174 0.1783 0.7811
n-Hexane 0.0922 0.0097 0.0427 0.0112 0.0490 0.0209 0.0917
Methylcyclopentane 0.2545 0.0269 0.1179 0.0309 0.1353 0.0578 0.2531
Benzene 0.0021 0.0002 0.0010 0.0003 0.0011 0.0005 0.0021
2-Methylhexane 0.0378 0.0040 0.0175 0.0046 0.0201 0.0086 0.0376
3-Methylhexane 0.4437 0.0469 0.2055 0.0538 0.2358 0.1008 0.4413
Heptane 0.7799 0.0825 0.3613 0.0946 0.4145 0.1771 0.7758
Methylcyclohexane 0.4564 0.0483 0.2114 0.0554 0.2426 0.1037 0.4540
Toluene 0.0100 0.0011 0.0046 0.0012 0.0053 0.0023 0.0099
Octane 0.6523 0.0690 0.3022 0.0792 0.3467 0.1481 0.6489
Ethylbenzene 0.0110 0.0012 0.0051 0.0013 0.0059 0.0025 0.0110
m & p-Xylene 0.0085 0.0009 0.0039 0.0010 0.0045 0.0019 0.0084
o-Xylene 0.0148 0.0016 0.0068 0.0018 0.0078 0.0034 0.0147
Nonane 0.1503 0.0159 0.0696 0.0182 0.0799 0.0341 0.1495
C10+ 0.0348 0.0037 0.0161 0.0042 0.0185 0.0079 0.0347
Total VOCs 67.463 7.1349 31.251 8.1867 35.8576 15.3216 67.108
Total CO2e 2.5404 11.1267 2.9148 12.7670 5.4552 23.894
Total TAPs (Benzene) 0.0002 0.0010 0.0003 0.0011 0.0005 0.0021
Toluene 0.0011 0.0046 0.0012 0.0053 0.0023 0.0099
Ethylbenzene 0.0012 0.0051 0.0013 0.0059 0.0025 0.0110
Xylenes 0.0025 0.0108 0.0028 0.0124 0.0053 0.0231
n-Hexane 0.0097 0.0427 0.0112 0.0490 0.0209 0.0917
Total HAPs 0.0147 0.0642 0.0168 0.0736 0.0315 0.1378
Total 100.00 10.5760 46.3230 12.1351 53.1516 22.7111 99.475
Condensate Tank W/B Losses
Working Losses Breathing Losses Max W/B Losses
Antero Resources Corporation
Table 7
Uncontrolled Working and Breathing Losses
Edna Monroe Well Pad
Tyler County, West Virginia
CRA 082715 (197)
Antero Resources Corporation
Table 7
Uncontrolled Working and Breathing Losses
Edna Monroe Well Pad
Tyler County, West Virginia
Produced Water Tank Information
Number of Tanks 2
Maximum Working Losses (lbs/hr) 0.5856
Maximum Breathing Losses (lbs/hr) 0.0082
Vapor Mass Fraction
wt% lbs/hr tpy lbs/hr tpy lbs/hr tpy
H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Nitrogen 0.0076 0.0000 0.0002 0.0000 0.0000 0.0000 0.0002
Carbon Dioxide 2.7173 0.0159 0.0697 0.0002 0.0010 0.0161 0.0707
Methane 3.3104 0.0194 0.0849 0.0003 0.0012 0.0197 0.0861
Ethane 1.0597 0.0062 0.0272 0.0001 0.0004 0.0063 0.0276
Propane 0.1030 0.0006 0.0026 0.0000 0.0000 0.0006 0.0027
Isobutane 0.0007 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
n-Butane 0.0038 0.0000 0.0001 0.0000 0.0000 0.0000 0.0001
Isopentane 0.0002 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
n-Pentane 0.0001 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
2-Methylpentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
3-Methylpentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
n-Hexane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Methylcyclopentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Benzene 0.0001 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
2-Methylhexane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
3-Methylhexane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Heptane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Methylcyclohexane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Toluene 0.0001 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Octane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Ethylbenzene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
m & p-Xylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
o-Xylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Nonane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
C10+ 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Total VOCs 0.1082 0.0006 0.0028 0.0000 0.0000 0.0006 0.0028
Total CO2e 0.5005 2.1923 0.0070 0.0307 0.5075 2.2230
Total TAPs (Benzene) 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Toluene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Ethylbenzene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Xylenes 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
n-Hexane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Total HAPs 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Total 100.00 0.5856 2.5648 0.0082 0.0360 0.5938 2.6008
Enter any notes here: Vapor mass fractions, working losses and breathing losses from Promax output
Working Losses Breathing Losses Max W/B Losses
Produced Water Tank W/B Losses
CRA 082715 (197)
Annual Loading Oil Truck Loading Water Truck Loading
RVP 2.65 1.0233
Annual Average Temp (F) 72.1 72.1
S (saturation factor) 0.6 0.6
P (true vapor pressure) 1.57 0.45
M (MW of vapor) 41.94 18.32
Collection Efficiency (%) 0 0
Loading Loss (lb/10^3 gal)* 0.92 0.12
Maximum Throughput (gallons/hr) 10,080 10,080
Average Throughput (gallons/yr) 17,629,500 211,554,000
Loading Emissions (lbs/hr) 9.31 1.16
Loading Emissions (tpy) 8.15 12.17
Vapor Mass Fraction Vapor Mass Fraction
wt% lbs/hr tpy wt% lbs/hr tpy
H2S 0.0000 0.00 0.00 0.0000 0.00E+00 0.00E+00
Nitrogen 0.0002 0.00 0.00 0.0076 8.77E-05 9.20E-04
Carbon Dioxide 0.1372 0.01 0.01 2.7173 3.15E-02 3.31E-01
Methane 0.9553 0.09 0.08 3.3104 3.84E-02 4.03E-01
Ethane 31.4443 2.93 2.56 1.0597 1.23E-02 1.29E-01
Propane 32.7228 3.05 2.67 0.1030 1.19E-03 1.25E-02
Isobutane 7.3520 0.68 0.60 0.0007 8.28E-06 8.69E-05
n-Butane 13.5387 1.26 1.10 0.0038 4.46E-05 4.68E-04
Isopentane 4.7333 0.44 0.39 0.0002 2.48E-06 2.61E-05
n-Pentane 3.7605 0.35 0.31 0.0001 1.39E-06 1.46E-05
2-Methylpentane 1.6221 0.15 0.13 0.0000 5.28E-08 5.54E-07
3-Methylpentane 0.7852 0.07 0.06 0.0000 1.65E-07 1.74E-06
n-Hexane 0.0922 0.01 0.01 0.0000 1.35E-09 1.42E-08
Methylcyclopentane 0.2545 0.02 0.02 0.0000 3.62E-07 3.80E-06
Benzene 0.0021 0.00 0.00 0.0001 9.72E-07 1.02E-05
2-Methylhexane 0.0378 0.00 0.00 0.0000 2.80E-10 2.94E-09
3-Methylhexane 0.4437 0.04 0.04 0.0000 3.41E-09 3.58E-08
Heptane 0.7799 0.07 0.06 0.0000 5.01E-09 5.25E-08
Methylcyclohexane 0.4564 0.04 0.04 0.0000 9.50E-08 9.97E-07
Toluene 0.0100 0.00 0.00 0.0001 9.80E-07 1.03E-05
Octane 0.6523 0.06 0.05 0.0000 5.15E-10 5.41E-09
Ethylbenzene 0.0110 0.00 0.00 0.0000 3.19E-07 3.35E-06
m & p-Xylene 0.0085 0.00 0.00 0.0000 2.11E-07 2.22E-06
o-Xylene 0.0148 0.00 0.00 0.0000 4.59E-07 4.82E-06
Nonane 0.1503 0.01 0.01 0.0000 9.55E-11 1.00E-09
C10+ 0.0348 0.00 0.00 0.0000 2.71E-12 2.85E-11
Total VOCs 67.4629 6.284 5.495 0.1082 1.25E-03 1.32E-02
Total CO2e 2.237 1.9564 0.9915 10.4049
Total TAPs (Benzene) 0.0002 0.0002 0.0000 0.0000
Toluene 0.0009 0.0008 0.0000 0.0000
Ethylbenzene 0.0010 0.0009 0.0000 0.0000
Xylenes 0.0022 0.0019 0.0000 0.0000
n-Hexane 0.0086 0.0075 0.0000 0.0000
Total HAPs 0.0129 0.0113 0.0000 0.0000
Total 100.0000 9.3141 8.1450 100.0000 1.1600 12.1728
Vapor mass fractions and loading losses from Promax output
*Using equation LL = 12.46* SPM/T from AP-42, Chapter 5, Section 5.2-4
MW was obtained by Promax; RVP was taken from laboratory reports
Annual Average Temp (F) obtained from Charleston, WV (preset in Promax)
S (saturation factor) is based on submerged loading, dedicated service as it was most representative
True vapor pressure (TVP) equation from AP-42, Chapter 7, Figure 7.1-13b
Loading emissions are vented to the atmosphere.
Enter any notes here
Loading Losses Loading Losses
Table 8
Loading Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
Condensate Tank Loading Losses Produced Water Tank Loading Losses
CRA 082715 (197)
Number of Units 10
GPU Heater Rating (MMBtu/hr) 1.50
Operating hours/year 8760
Fuel Heat Value (Btu/scf) 1,247
Emission Factors
(lb/MMscf)
NOx 100 1.203 5.268
CO 84 1.010 4.425
CO2 120,000 1443.395 6322.070
Lead 0.0005 6.01E-06 2.63E-05
N2O 2.2 0.026 0.116
PM (Total) 7.6 0.091 0.400
SO2 0.6 0.007 0.032
TOC 11 0.132 0.580
Methane 2.3 0.028 0.121
VOC 5.5 0.066 0.290
2-Methylnaphthalene 2.40E-05 2.89E-07 1.26E-06
Benzene 2.10E-03 2.53E-05 1.11E-04
Dichlorobenzene 1.20E-03 1.44E-05 6.32E-05
Fluoranthene 3.00E-06 3.61E-08 1.58E-07
Fluorene 2.80E-06 3.37E-08 1.48E-07
Formaldehyde 7.50E-02 9.02E-04 3.95E-03
Hexane 1.80E+00 2.17E-02 9.48E-02
Naphthalene 6.10E-04 7.34E-06 3.21E-05
Phenanathrene 1.70E-05 2.04E-07 8.96E-07
Toluene 3.40E-03 4.09E-05 1.79E-04
lb/hr tpy
TOTAL Uncontrolled VOC 0.066 0.290
TOTAL Uncontrolled HAPs 0.023 0.099
TOTAL Uncontrolled TAPs (Benzene) 0.000 0.000
TOTAL Uncontrolled TAPs (Formaldehyde) 0.001 0.004
TOTAL CO2e Emissions 1,451.97 6,359.64
Enter any notes here:
All Emission Factors based off AP-42 Sec 1.4 Natural Gas Combustion
Antero Resources Corporation
HAPS
Pollutant lb/hr tpy
Table 9
Gas Production Unit Heater Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
CRA 082715 (197)
Unit Name:
Pollutant
NOx 1,000,000
CO 1,000,000
PM10 2,000
PM2.5 34.08
SO2 64.06
CO2 seconds/hour 3,600
VOC 12
benzene
Hexane
Toluene
Formaldehyde
N2O
Lead
VOC percent destruction
efficiency (%)98
H2S percent destruction
efficiency (%)98
Enclosed Combustor
operating hours
8760
1 2 3 4 5 6 Total
Stream Sent to Enclosed
Combustor/Vapor Combustor
(Enter Name of Each Stream
Here)
pilot(s)added fuel
stream(s)
Oil Tank Flash
Emissions
Water Tank Flash
Emissions
Oil Tank W/B
Emissions
Water Tank
W/B
Emissions
-
Maximum Expected Hourly
Volumetric Flow Rate of
Stream (scf/hr)
12.6 -- 3,275.73 1,773.28 205.51 12.30 5,279.42
Maximum Expected Annual
Volumetric Flow Rate of
Stream (scf/yr)
110,376.00 -- 28,695,426.58 15,533,942.40 1,800,227.70 107,715.21 46,247,687.89
Heating Content (Btu/ft3) 1,247 2,178.24 1,052.77 2,178.24 1,052.77 1,792.39
1 2 3 4 5 6 Total
Stream Sent to Enclosed
Combustor/Vapor Combustor
pilot(s)added fuel
stream(s)
Oil Tank Flash
Emissions
Water Tank Flash
Emissions
Oil Tank W/B
Emissions
Water Tank
W/B
Emissions
-
H2S - - 0.000 0.000 0.000 0.000 0.000
Total VOC - - 254.191 10.693 15.322 0.001 280.21
Benzene - - 0.150 0.058 0.000 0.000 0.208
Toluene - - 0.334 0.121 0.002 0.000 0.457
Ethylbenzene - - 0.196 0.070 0.003 0.000 0.269
Xylenes - - 0.353 0.128 0.005 0.000 0.486
n-Hexane - - 5.528 0.033 0.021 0.000 5.582
HAPs - - 6.560 0.410 0.031 0.000 7.001
Total Mass Flow - - 362.012 85.631 22.711 0.594 470.948
H2S - - 0.000 0.000 0.000 0.000 0.000
Total VOC - - 1113.358 46.836 67.108 0.003 1227.306
Benzene - - 0.657 0.253 0.002 0.000 0.911
Toluene - - 1.463 0.530 0.010 0.000 2.002
Ethylbenzene - - 0.859 0.307 0.011 0.000 1.176
Xylenes - - 1.545 0.560 0.023 0.000 2.128
n-Hexane - - 24.212 0.145 0.092 0.000 24.449
HAP - - 28.734 1.794 0.138 0.000 30.666
Total Mass Flow - - 1585.614 375.062 99.475 2.601 2062.752
Constants
120,000
5.5
2.10E-03
inches/ft
Destruction Efficiency
Stream Information
Mass Flow Rates of the Vapors Sent to this Control Device, Hourly Basis (lb/hr)
Mass Flow Rates of the Vapors Sent to this Control Device, Annual Basis (tpy)
2.20
5.00E-04
1.80E+00
3.40E-03
7.50E-02
Table 10
Enclosed Combustor Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
5.7 H2S molecular weight
0.6 SO2 molecular weight
100 Btu/MMBtu
84 scf/MMscf
7.6 lb/ton
General Information
EC001
Emission Factor (lb/MMscf)
CRA 082715 (197)
Table 10
Enclosed Combustor Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
1 2 3 4 5 6 Total
Stream Sent to Enclosed
Combustor/Vapor Combustor
pilot(s)added fuel
stream(s)
Oil Tank Flash
Emissions
Water Tank Flash
Emissions
Oil Tank W/B
Emissions
Water Tank
W/B
Emissions
-
NOx 0.001 - 0.328 0.177 0.021 0.001 0.53
CO 0.001 - 0.275 0.149 0.017 0.001 0.44
PM2.5 0.000 - 0.019 0.010 0.001 0.000 0.03
PM10 0.000 - 0.025 0.013 0.002 0.000 0.04
H2S 0.000 - 0.000 0.000 0.000 0.000 0.00
SO2 0.000 - 0.000 0.000 0.000 0.000 0.00
CO2 1.512 - - - - - 1.51
Total VOC 0.000 - 5.084 0.214 0.306 0.000 5.60
Benzene 0.000 - 0.003 0.001 0.000 0.000 0.00
Toluene 0.000 - 0.007 0.002 0.000 0.000 0.01
Ethylbenzene 0.000 - 0.004 0.001 0.000 0.000 0.01
Xylenes 0.000 - 0.007 0.003 0.000 0.000 0.01
n-Hexane 0.000 - 0.111 0.001 0.000 0.000 0.11
HAP 0.000 - 0.131 0.008 0.001 0.000 0.14
N2O 0.000 - 0.007 0.004 0.000 0.000 0.01
Lead 0.000 - 0.000 0.000 0.000 0.000 0.00
Formaldehyde 0.000 - - - - - 0.00
1 2 3 4 5 6 Total
Stream Sent to Enclosed
Combustor/Vapor Combustor
pilot(s)added fuel
stream(s)
Oil Tank Flash
Emissions
Water Tank Flash
Emissions
Oil Tank W/B
Emissions
Water Tank
W/B
Emissions
-
NOx 0.006 - 1.435 0.777 0.090 0.005 2.31
CO 0.005 - 1.205 0.652 0.076 0.005 1.94
PM2.5 0.000 - 0.082 0.044 0.005 0.000 0.13
PM10 0.000 - 0.109 0.059 0.007 0.000 0.18
H2S 0.000 - 0.000 0.000 0.000 0.000 0.00
SO2 0.000 - 0.000 0.000 0.000 0.000 0.00
CO2 6.623 - - - - - 6.62
Total VOC 0.000 - 22.267 0.937 1.342 0.000 24.55
Benzene 0.000 - 0.013 0.005 0.000 0.000 0.02
Toluene 0.000 - 0.029 0.011 0.000 0.000 0.04
Ethylbenzene 0.000 - 0.017 0.006 0.000 0.000 0.02
Xylenes 0.000 - 0.031 0.011 0.000 0.000 0.04
n-Hexane 0.000 - 0.484 0.003 0.002 0.000 0.49
HAP 0.000 - 0.575 0.036 0.003 0.000 0.61
N2O 0.000 - 0.032 0.017 0.002 0.000 0.05
Lead 0.000 - 0.000 0.000 0.000 0.000 0.00
Formaldehyde 0.000 - - - - - 0.00
Hourly
Emissions
(lb/hr)
Annual
Emissions
(tpy)
Total VOC 5.60 24.55
NOx 5.28E-01 2.31E+00
CO 4.43E-01 1.94E+00
PM2.5 3.01E-02 1.32E-01
PM10 4.01E-02 1.76E-01
H2S 4.02E-06 1.76E-05
SO2 7.56E-06 3.31E-05
Benzene (TAPs) 4.16E-03 1.82E-02
Formaldehyde (TAPs) 9.45E-07 4.14E-06
HAPs 0.14 0.61
CO2e 2679.58 11736.54
N2O 1.16E-02 5.09E-02
Lead 2.64E-06 1.16E-05
Enclosed Combustor/Vapor Combustor Total Emissions
Enter any notes here as needed
1. Emission Factors from AP-42 Tables 1.4-1, 1.4-2, and 1.4.3
Annual (tpy)
Controlled Emissions
Hourly (lb/hr)
CRA 082715 (197)
Enclosed Combustor CO2 and CH4 Emissions
Mole fraction of
oil flash gas
constituentsa
Volume of oil
flash gas sent
to flare
Mole fraction
of water flash
gas
constituentsa
Volume of
water flash gas
sent to flare
Mole fraction
of oil tank
vapors
constituentsa
Volume of oil
tank vapor sent
to flare
Mole fraction
of water tank
vapors
constituentsa
Volume of
water tank
vapors sent to
flare
Component
volume of gas
sent to flare
Number of
carbon atoms
Combustion
Efficiency
Combusted
CO2 Volumeb
Uncombusted
CO2 and CH4
Volumeb
Volume GHGs
Emitted
scf/year scf/year scf/year scf/year scf/year scf/year scf/year scf/year
CO2 0.001 28,695,427 0.0470 15,533,942 0.0013 1,800,228 0.011 107,715 768,203 1 0 -- 768,203 176,970,910
Methane 0.115 28,695,427 3.8061 15,533,942 0.0250 1,800,228 0.038 107,715 62,475,745 1 0.98 61,226,231 1,249,515 1,249,515
Ethane 0.347 28,695,427 0.7042 15,533,942 0.4386 1,800,228 0.006 107,715 21,673,620 2 0.98 42,480,295 --
Propane 0.290 28,695,427 0.1914 15,533,942 0.3112 1,800,228 0.000 107,715 11,845,459 3 0.98 34,825,648 --
i-Butane 0.053 28,695,427 0.0080 15,533,942 0.0530 1,800,228 0.000 107,715 1,746,367 4 0.98 6,845,759 --
n-Butane 0.100 28,695,427 0.0288 15,533,942 0.0977 1,800,228 0.000 107,715 3,481,178 4 0.98 13,646,216 --
Pentane 0.053 28,695,427 0.0091 15,533,942 0.0494 1,800,228 0.000 107,715 1,762,812 5 0.98 8,637,781 --
Hexane 0.020 28,695,427 0.0019 15,533,942 0.0122 1,800,228 0.000 107,715 637,388 6 0.98 3,747,840 --
Benzene 0.000 28,695,427 0.0008 15,533,942 0.0000 1,800,228 0.000 107,715 19,300 6 0.98 113,485 --
Heptanes 0.011 28,695,427 0.0015 15,533,942 0.0065 1,800,228 0.000 107,715 339,638 7 0.98 2,329,920 --
Toluene 0.000 28,695,427 0.0015 15,533,942 0.0000 1,800,228 0.000 107,715 35,046 7 0.98 240,414 --
Octane 0.006 28,695,427 0.0011 15,533,942 0.0043 1,800,228 0.000 107,715 187,132 8 0.98 1,467,115 --
Ethyl benzene 0.000 28,695,427 0.0007 15,533,942 0.0000 1,800,228 0.000 107,715 17,731 8 0.98 139,011 --
Xylenes 0.000 28,695,427 0.0014 15,533,942 0.0001 1,800,228 0.000 107,715 32,226 8 0.98 252,652 --
Nonane 0.001 28,695,427 0.0000 15,533,942 0.0005 1,800,228 0.000 107,715 22,621 9 0.98 199,520 --
Decane plus 0.000 28,695,427 0.0000 15,533,942 0.0001 1,800,228 0.000 107,715 5,186 10 0.98 50,821 --
176,202,707 --
Volume EmittedDensity of
GHGc
Conversion
Factor
scf/year lb/scf lb/ton lbs/hr (tons/yr)
CO2 176,970,910 0.12 2000 1 2342.70 10,261.04
CH4 1,249,515 0.09 2000 25 13.27 58.12
2,674.5 11714.15
GHG Emissions Summary
Notes
a Flashing/Working/Breathing Losses from ProMax output reports
b 40 CFR 98.233 (n)(4): Eqns: W-19, W-20 and W-21
c 40 CFR 98.233(v) Eqn W-36 - density at 60F and 14.7 psia
Subtotal
CO2e Emissions
Emissionsc
GWF
Components
Pollutant
Antero Resources Corporation
Table 11
Enclosed Combustor GHG Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
CRA 082715 (197)
PM PM10
Particle Size Multiplier (k) 0.8 0.36
Silt Content of Road Surface Material (s) (%) 5.1 5.1
Days per Year with Precipitation > 0.01 in (p) 150 150
Control Efficiency for Watering 1
(%) 50 50
Condensate Production (bbl/day) 1150
PW Production (bbl/day) 13,800
Truck Capacity (bbl) 200
No of Trips Per day 2
Trips Per Year 730
# of
Wheels
Mean Vehicle
Weight (W)
Mean Vehicle
Speed (S)
Miles Per
Trip
Maximum
Trips per
Hour
Maximum
Trips per
Year
PM PM10
(tons) (mph) (miles) (miles/hr) (miles/year) (lbs/VMT) (lbs/VMT)
Tanker Trucks Condensate 10 40 10 0.1600 1 2099 0.1600 335.8400 3.8175 1.7179
Tanker Trucks PW 10 40 10 0.1600 1 25185 0.1600 4029.6000 3.8175 1.7179
Pick Up Truck 4 3 10 0.3100 1 730 0.3100 226.3000 0.3467 0.1560
(lbs/hr) (lbs/year) (tpy) (lbs/hr) (lbs/year) (tpy) (lbs/hr) (lbs/year) (tpy) (lbs/hr) (lbs/year) (tpy)
Tanker Trucks Condensate 0.6108 1282.0791 0.6410 0.2749 576.9356 0.2885 0.3054 641.0395 0.3205 0.1374 288.4678 0.1442
Tanker Trucks PW 0.6108 15383.1164 7.6916 0.2749 6922.4024 3.4612 0.3054 7691.5582 3.8458 0.1374 3461.2012 1.7306
Pick Up Truck 0.1075 78.4536 0.0392 0.0484 35.3041 0.0177 0.0537 39.2268 0.0196 0.0242 17.6521 0.0088
Total Emissions 1.3291 16,743.6491 8.3718 0.5981 7,534.6421 3.7673 0.6645 8,371.8246 4.1859 0.2990 3,767.3211 1.8837
Haul Road Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
Table 12
Vehicle Miles Travelled
Tanker Truck Trip Calculation
Pick Up Truck Trip Calculation
PM10
Uncontrolled Emissions
PM PM PM10
Controlled Emissions
1 EPA, AP-42, Volume I, Section 13.2.2 Unpaved Roads (11/06); assume 2:1 moisture ratio Section 13.2.2 Unpaved Roads (11/06)
Source: Attachment L, Fugitive Emissions from Unpaved Haul Roads, Rev 03/2007, West Virginia Department of Environmental ProtectionEnter any notes here:
CRA 082715 (197)
Kubota DG972-E2
24
0.449
Heat Content of Fuel (Btu/scf) 1247.06
0.056
8760
(g/hp-hr) (lb/MMBtu)
NOx1
5.97 0.3158 1.3831
CO2
106.7 5.6445 24.7228
CO2 110.000 26.3967 115.62
PM2.5 9.910E-03 0.0024 0.0104
PM10 9.500E-03 0.0023 0.0100
PM (Total) 9.910E-03 0.0024 0.0104
SO2 5.880E-04 0.0001 0.0006
TOC 0.358 0.0859 0.3763
Methane 0.230 0.0552 0.2417
VOC3
0.0296 0.0071 0.0311
Benzene 1.58E-03 3.79E-04 1.66E-03
Ethylbenzene 2.48E-05 5.95E-06 2.61E-05
Formaldehyde 2.05E-02 4.92E-03 2.15E-02
Naphthalene 9.71E-05 2.33E-05 1.02E-04
Toluene 5.58E-04 1.34E-04 5.86E-04
Xylene 1.95E-04 4.68E-05 2.05E-04
lb/hr tpy
0.007 0.031
0.316 1.383
0.006 0.024
0.000 0.002
0.005 0.022
27.78 121.7
Enter Any Notes Here:
2. Emission factor for CO was the Certification CO level taken from EPA's Non-
Road Small SI 2013 Certification issued by Office of Transportation and Air
Quality, March 2014.
3. Emission factors for all other contaminants including VOCs were obtained
from AP-42, Section 3.2 "Natural Gas-fired Reciprocating Engines", Table 3.2-3.
Fuel consumption (lbs/BHP-hr) 1
Density of NG (lb/scf)
TOTAL CO2e Emissions
HAPS
TOTAL Uncontrolled NOx
TOTAL Uncontrolled HAPs
TOTAL Uncontrolled TAPs (Benzene)
TOTAL Uncontrolled TAPs (Formaldehyde)
1. Emission factor used for the 24 HP engine's Nox is the 40 CFR 1054 standard
indicated on the EPA's Certificate of Conformity. See Appendix P.
TOTAL Uncontrolled VOC
Power (hp)
Emission Factorstpy
Operating Hours/year
lb/hrPollutant
Table 13
Engine Emissions
Edna Monroe Well Pad
Tyler County, West Virginia
Antero Resources Corporation
CRA 082715 (197)
Client Name:
Location:
Job:
Project Name:
File Name:
ProMax Version:
Report Created:
3.2.13330.0
5/13/2015 11:46
Simulation Report
Antero Resources Corporation
West Virginia
Edna Monroe Well Pad
PROMAX SCENARIO 3
ProMax@C:\Users\yichen\Documents\New Model\Antero ProMax\Antero
WV_Updated 2Ph Separator\PROMAX SCENARIO 3.PMX
Properties
Pressure(Total)
Temperature(Total)
Std Vapor Volumetric Flow(Total)
HP Separator Gas
232*
70*
200
psig
°F
MMSCFD
Names
Std Liquid Volumetric Flow
Reid Vapor Pressure
Units
bbl/d
psi
Sales Oil
1150
10.733
Produced Water
13800
1.0233
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Total Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Mole Fraction % % % % % % % % % % % % % % % %
Water 33.8263 0.157552 99.9588 0.0501987 0.229379 0.00462880 0 100 0 99.9969 3.02994 0.000109874 99.9589 98.8029 0.0214883
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 0.327334 0.493930 0.000112685 0.0142266 0.00911088 1.35784E-05 0.494658 0 0.016 3.26005E-06 0.278296 0.000339243 0.000101795 0.000285662 0.000696006
Carbon Dioxide 0.0970882 0.145923 0.000829929 0.0285456 0.122484 0.00212169 0.146717 0 0 0.000458380 0.945391 0.130788 0.00116544 0.00115196 0.0111506
Methane 51.4182 77.5798 0.0319662 6.36327 11.5107 0.0549825 77.7018 0 6.555 0.00184397 76.6094 2.49734 0.0310988 0.106549 0.914323
Ethane 9.39691 14.1779 0.00597218 6.55557 34.6571 1.05871 14.2004 0 6.561 0.000397706 14.1775 43.8560 0.00607361 0.0818830 3.57907
Propane 2.97406 4.48715 0.00163468 5.98557 28.9707 3.33530 4.49433 0 5.95 0.000119446 3.85371 31.1216 0.00203453 0.0708243 5.25832
Isobutane 0.374984 0.565850 6.53738E-05 1.82784 5.31811 1.57239 0.566666 0 1.825 1.74525E-06 0.161824 5.30483 8.17882E-05 0.0211874 1.85337
n-Butane 0.783456 1.18213 0.000241498 4.46074 9.96142 4.23308 1.18394 0 4.446 1.37563E-05 0.579212 9.76878 0.000367047 0.0517820 4.66279
Isopentane 0.248114 0.374394 4.24621E-05 2.96090 2.96077 3.25618 0.374944 0 2.955 1.68795E-06 0.103699 2.75134 7.47499E-05 0.0342492 3.23402
n-Pentane 0.192853 0.291007 3.25188E-05 3.11443 2.38069 3.51139 0.291434 0 3.109 1.28046E-06 0.0794474 2.18589 5.64763E-05 0.0360122 3.42657
2-Methylpentane 0 0 5.30992E-06 2.68359 0.878065 3.16144 0 0 2.681 1.01661E-07 0.0132459 0.789398 0 0.0310065 2.99016
3-Methylpentane 0 0 7.09285E-06 1.44904 0.426199 1.71255 0 0 1.448 3.56740E-07 0.0171318 0.382131 0 0.0167465 1.61605
n-Hexane 0.360755 0.544400 3.50085E-06 3.10340 0.735656 3.68797 0.545164 0 3.097 5.35076E-08 0.00876741 0.0448536 3.68296E-05 0.0358540 3.46651
Methylcyclopentane 0 0 8.14194E-06 0.667069 0.152715 0.793339 0 0 0.667 1.11693E-06 0.0178673 0.126811 0 0.00771403 0.745283
Benzene 0 0 5.89487E-05 0.0970732 0.0220101 0.115470 0 0 0.102 5.23633E-05 0.0168004 0.00113757 0 0.00117966 0.108459
2-Methylhexane 0 0 1.47359E-06 2.71802 0.277903 3.27161 0 0 2.715 2.39339E-08 0.00368683 0.0158226 0 0.0313997 3.04704
3-Methylhexane 0 0 1.19900E-06 2.22348 0.216512 2.67755 0 0 2.221 2.03400E-08 0.00299762 0.185684 0 0.0256864 2.49294
Heptane 0 0 2.39859E-06 5.34300 0.413355 6.44617 0 0 5.337 4.09139E-08 0.00599613 0.326405 0 0.0617238 5.99363
Methylcyclohexane 0 0 8.16811E-06 3.13194 0.244552 3.77836 0 0 3.129 7.77571E-07 0.0187966 0.194948 0 0.0361877 3.51327
Toluene 0 0 8.86372E-05 0.655187 0.0415656 0.791497 0 0 0.662 7.69279E-05 0.0298562 0.00453880 0 0.00765620 0.735241
Octane 0 0 1.10485E-06 13.2093 0.322359 16.0157 0 0 13.194 1.25097E-08 0.00277808 0.239478 0 0.152592 14.8385
Ethylbenzene 0 0 4.08593E-05 1.00668 0.0211736 1.22094 0 0 1.009 3.49733E-05 0.0150046 0.00435350 0 0.0116693 1.13094
m-Xylene 0 0 2.49320E-05 0.718709 0.0126632 0.871953 0 0 0.72 2.14459E-05 0.00888734 0.00335273 0 0.00832699 0.807494
o-Xylene 0 0 6.75755E-05 1.61611 0.0254362 1.96105 0 0 1.62 6.03279E-05 0.0184926 0.00583152 0 0.0187357 1.81585
Nonane 0 0 3.89733E-07 9.13965 0.0731056 11.0983 0 0 9.129 6.97170E-09 0.000973456 0.0491355 0 0.105579 10.2713
C10+ 0 0 9.80662E-08 20.8764 0.0162823 25.3673 0 0 20.852 1.95336E-09 0.000244438 0.00917666 0 0.241159 23.4656
Molar Flow lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h
Water 11209.8 34.5978 11175.2 0.0655883 0.0200008 0.00497684 0 11209.8 0 11175.0 0.133193 5.95014E-07 0 11175.2 11175.2 0.0249777
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 108.477 108.465 0.0125980 0.0185881 0.000794428 1.45994E-05 108.477 0 0.0209297 0.000364323 0.0122336 1.83714E-06 0 0.0113805 0.0323102 0.000809027
Carbon Dioxide 32.1745 32.0442 0.0927842 0.0372970 0.0106801 0.00228122 32.1745 0 0 0.0512257 0.0415585 0.000708274 0 0.130294 0.130294 0.0129613
Methane 17039.7 17036.2 3.57375 8.31409 1.00368 0.0591167 17039.7 0 8.57463 0.206071 3.36768 0.0135241 0 3.47679 12.0514 1.06280
Ethane 3114.08 3113.40 0.667677 8.56534 3.02195 1.13831 3114.08 0 8.58248 0.0444452 0.623232 0.237498 0 0.679019 9.26150 4.16026
Propane 985.588 985.361 0.182754 7.82059 2.52611 3.58608 985.588 0 7.78323 0.0133485 0.169405 0.168536 0 0.227457 8.01068 6.11220
Isobutane 124.268 124.259 0.00730865 2.38821 0.463715 1.69062 124.268 0 2.38729 0.000195038 0.00711361 0.0287279 0 0.00914378 2.39644 2.15434
n-Butane 259.633 259.592 0.0269989 5.82829 0.868591 4.55136 259.633 0 5.81584 0.00153732 0.0254616 0.0529021 0 0.0410352 5.85687 5.41995
Isopentane 82.2237 82.2154 0.00474716 3.86863 0.258166 3.50101 82.2237 0 3.86545 0.000188635 0.00455853 0.0148997 0 0.00835691 3.87381 3.75918
n-Pentane 63.9104 63.9040 0.00363553 4.06924 0.207586 3.77541 63.9104 0 4.06690 0.000143096 0.00349243 0.0118375 0 0.00631396 4.07321 3.98299
2-Methylpentane 0 0 0.000593637 3.50631 0.0765633 3.39915 0 0 3.50703 1.13611E-05 0.000582276 0.00427492 0 0 3.50703 3.47571
3-Methylpentane 0 0 0.000792965 1.89328 0.0371627 1.84131 0 0 1.89414 3.98670E-05 0.000753098 0.00206940 0 0 1.89414 1.87848
n-Hexane 119.552 119.548 0.000391387 4.05482 0.0641459 3.96527 119.552 0 4.05120 5.97968E-06 0.000385407 0.000242901 0 0.00411749 4.05532 4.02942
Methylcyclopentane 0 0 0.000910250 0.871575 0.0133161 0.852990 0 0 0.872506 0.000124821 0.000785430 0.000686734 0 0 0.872506 0.866306
Benzene 0 0 0.00659033 0.126833 0.00191918 0.124152 0 0 0.133427 0.00585180 0.000738531 6.16043E-06 0 0 0.133427 0.126071
2-Methylhexane 0 0 0.000164744 3.55130 0.0242319 3.51760 0 0 3.55151 2.67471E-06 0.000162070 8.56861E-05 0 0 3.55151 3.54183
3-Methylhexane 0 0 0.000134045 2.90514 0.0188789 2.87887 0 0 2.90530 2.27307E-06 0.000131772 0.00100556 0 0 2.90530 2.89775
Heptane 0 0 0.000268157 6.98103 0.0360427 6.93086 0 0 6.98136 4.57228E-06 0.000263584 0.00176762 0 0 6.98136 6.96690
Methylcyclohexane 0 0 0.000913176 4.09211 0.0213238 4.06245 0 0 4.09306 8.68966E-05 0.000826280 0.00105572 0 0 4.09306 4.08378
Toluene 0 0 0.00990944 0.856050 0.00362434 0.851009 0 0 0.865966 0.00859699 0.00131245 2.45795E-05 0 0 0.865966 0.854634
Octane 0 0 0.000123520 17.2590 0.0281082 17.2199 0 0 17.2591 1.39801E-06 0.000122122 0.00129687 0 0 17.2591 17.2480
Ethylbenzene 0 0 0.00456798 1.31531 0.00184625 1.31274 0 0 1.31988 0.00390840 0.000659586 2.35760E-05 0 0 1.31988 1.31459
m-Xylene 0 0 0.00278734 0.939046 0.00110417 0.937515 0 0 0.941836 0.00239666 0.000390679 1.81564E-05 0 0 0.941836 0.938619
o-Xylene 0 0 0.00755479 2.11157 0.00221792 2.10850 0 0 2.11913 0.00674187 0.000812919 3.15801E-05 0 0 2.11913 2.11071
Nonane 0 0 4.35713E-05 11.9416 0.00637448 11.9328 0 0 11.9417 7.79114E-07 4.27922E-05 0.000266089 0 0 11.9417 11.9392
C10+ 0 0 1.09636E-05 27.2766 0.00141975 27.2746 0 0 27.2766 2.18296E-07 1.07453E-05 4.96955E-05 0 0 27.2766 27.2761
Mass Fraction % % % % % % % % % % % % % % % %
Water 30.5974 0.135912 99.9524 0.00921427 0.0995326 0.000742758 0 100 0 99.9949 2.72578 4.71987E-05 99.9520 93.9685 0.00361920
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 0.460411 0.662560 0.000175212 0.00406065 0.00614747 3.38807E-06 0.663391 0 0.00457137 5.06921E-06 0.389305 0.000226605 0.000158278 0.000422464 0.000182284
Carbon Dioxide 0.214537 0.307514 0.00202730 0.0128001 0.129837 0.000831699 0.309119 0 0 0.00111975 2.07766 0.137249 0.00284685 0.00267643 0.00458791
Methane 41.4168 59.5955 0.0284638 1.04011 4.44777 0.00785659 59.6762 0 1.07252 0.00164201 61.3719 0.955306 0.0276913 0.0902389 0.137133
Ethane 14.1871 20.4138 0.00996744 2.00843 25.1005 0.283553 20.4417 0 2.01210 0.000663792 21.2881 31.4443 0.0101367 0.129983 1.00614
Propane 6.58468 9.47457 0.00400092 2.68923 30.7698 1.30999 9.48766 0 2.67592 0.000292359 8.48577 32.7228 0.00497952 0.164873 2.16777
Isobutane 1.09432 1.57484 0.000210900 1.08245 7.44509 0.814031 1.57677 0 1.08185 5.63053E-06 0.469678 7.35203 0.000263853 0.0650118 1.00711
n-Butane 2.28637 3.29005 0.000779088 2.64166 13.9455 2.19148 3.29435 0 2.63556 4.43808E-05 1.68111 13.5387 0.00118411 0.158888 2.53371
Isopentane 0.898815 1.29345 0.000170044 2.17660 5.14522 2.09255 1.29507 0 2.17444 6.75989E-06 0.373613 4.73333 0.000299343 0.130452 2.18143
n-Pentane 0.698625 1.00537 0.000130225 2.28947 4.13717 2.25655 1.00663 0 2.28776 5.12795E-06 0.286237 3.76055 0.000226165 0.137167 2.31131
2-Methylpentane 0 0 2.53981E-05 2.35628 1.82255 2.42665 0 0 2.35636 4.86284E-07 0.0570007 1.62208 0 0.141061 2.40906
3-Methylpentane 0 0 3.39262E-05 1.27231 0.884640 1.31451 0 0 1.27266 1.70641E-06 0.0737230 0.785217 0 0.0761867 1.30199
n-Hexane 1.56094 2.24644 1.67451E-05 2.72489 1.52696 2.83080 2.24910 0 2.72198 2.55946E-07 0.0377287 0.0921668 0.000176161 0.163115 2.79284
Methylcyclopentane 0 0 3.80331E-05 0.572007 0.309568 0.594703 0 0 0.572519 5.21768E-06 0.0750894 0.254480 0 0.0342733 0.586400
Benzene 0 0 0.000255577 0.0772580 0.0414104 0.0803383 0 0 0.0812602 0.000227036 0.0655321 0.00211880 0 0.00486457 0.0792048
2-Methylhexane 0 0 8.19567E-06 2.77496 0.670718 2.91995 0 0 2.77464 1.33119E-07 0.0184479 0.0378049 0 0.166101 2.85446
3-Methylhexane 0 0 6.66847E-06 2.27005 0.522552 2.38975 0 0 2.26979 1.13130E-07 0.0149992 0.443654 0 0.135879 2.33538
Heptane 0 0 1.33402E-05 5.45493 0.997631 5.75329 0 0 5.45424 2.27561E-07 0.0300029 0.779877 0 0.326513 5.61482
Methylcyclohexane 0 0 4.45146E-05 3.13322 0.578351 3.30439 0 0 3.13340 4.23780E-06 0.0921606 0.456417 0 0.187578 3.22502
Toluene 0 0 0.000453302 0.615083 0.0922456 0.649573 0 0 0.622099 0.000393437 0.137370 0.00997185 0 0.0372414 0.633346
Octane 0 0 7.00501E-06 15.3739 0.886920 16.2952 0 0 15.3713 7.93179E-08 0.0158466 0.652279 0 0.920192 15.8465
Ethylbenzene 0 0 0.000240771 1.08893 0.0541436 1.15455 0 0 1.09253 0.000206095 0.0795465 0.0110208 0 0.0654033 1.12251
m-Xylene 0 0 0.000146916 0.777431 0.0323813 0.824542 0 0 0.779605 0.000126379 0.0471162 0.00848737 0 0.0466704 0.801476
o-Xylene 0 0 0.000398201 1.74816 0.0650436 1.85442 0 0 1.75411 0.000355508 0.0980385 0.0147624 0 0.105008 1.80232
Nonane 0 0 2.77443E-06 11.9435 0.225837 12.6786 0 0 11.9415 4.96322E-08 0.00623459 0.150267 0 0.714867 12.3160
C10+ 0 0 8.66550E-07 33.8631 0.0624354 35.9712 0 0 33.8572 1.72614E-08 0.00194325 0.0348355 0 2.02683 34.9257
Mass Flow lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h
Water 201948 623.289 201324 1.18159 0.360321 0.0896591 0 201948 0 201321 2.39951 1.07193E-05 0 201325 201325 0.449980
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 3038.80 3038.48 0.352912 0.520717 0.0222546 0.000408978 3038.80 0 0.586312 0.0102059 0.342706 5.14646E-05 0 0.318807 0.905118 0.0226636
Carbon Dioxide 1415.98 1410.25 4.08339 1.64142 0.470025 0.100395 1415.98 0 0 2.25442 1.82897 0.0311708 0 5.73418 5.73418 0.570420
Methane 273359 273303 57.3317 133.378 16.1015 0.948377 273359 0 137.558 3.30589 54.0258 0.216960 0 55.7763 193.334 17.0499
Ethane 93637.5 93617.1 20.0764 257.552 90.8670 34.2279 93637.5 0 258.067 1.33642 18.7400 7.14135 0 20.4174 278.484 125.095
Propane 43460.1 43450.1 8.05865 344.854 111.391 158.130 43460.1 0 343.206 0.588612 7.47004 7.43172 0 10.0298 353.236 269.521
Isobutane 7222.71 7222.18 0.424795 138.808 26.9522 98.2626 7222.71 0 138.755 0.0113360 0.413459 1.66973 0 0.531456 139.286 125.215
n-Butane 15090.4 15088.1 1.56924 338.753 50.4844 264.535 15090.4 0 338.029 0.0893526 1.47988 3.07478 0 2.38506 340.414 315.020
Isopentane 5932.34 5931.74 0.342502 279.117 18.6263 252.594 5932.34 0 278.888 0.0136098 0.328892 1.07499 0 0.602941 279.491 271.220
n-Pentane 4611.05 4610.60 0.262299 293.591 14.9771 272.391 4611.05 0 293.422 0.0103242 0.251975 0.854062 0 0.455544 293.877 287.368
2-Methylpentane 0 0 0.0511569 302.158 6.59787 292.923 0 0 302.220 0.000979043 0.0501778 0.368393 0 0 302.220 299.521
3-Methylpentane 0 0 0.0683341 163.154 3.20251 158.676 0 0 163.228 0.00343555 0.0648985 0.178331 0 0 163.228 161.878
n-Hexane 10302.5 10302.1 0.0337279 349.426 5.52779 341.709 10302.5 0 349.114 0.000515301 0.0332126 0.0209321 0 0.354826 349.469 347.237
Methylcyclopentane 0 0 0.0766062 73.3513 1.12067 71.7872 0 0 73.4297 0.0105048 0.0661014 0.0577952 0 0 73.4297 72.9078
Benzene 0 0 0.514783 9.90719 0.149911 9.69772 0 0 10.4222 0.457095 0.0576880 0.000481203 0 0 10.4222 9.84763
2-Methylhexane 0 0 0.0165077 355.847 2.42808 352.470 0 0 355.868 0.000268011 0.0162397 0.00858592 0 0 355.868 354.898
3-Methylhexane 0 0 0.0134316 291.100 1.89170 288.469 0 0 291.117 0.000227766 0.0132038 0.100759 0 0 291.117 290.360
Heptane 0 0 0.0268698 699.513 3.61155 694.486 0 0 699.546 0.000458152 0.0264117 0.177119 0 0 699.546 698.097
Methylcyclohexane 0 0 0.0896612 401.788 2.09370 398.876 0 0 401.882 0.00853203 0.0811291 0.103657 0 0 401.882 400.970
Toluene 0 0 0.913040 78.8751 0.333941 78.4107 0 0 79.7887 0.792113 0.120927 0.00226472 0 0 79.7887 78.7446
Octane 0 0 0.0141095 1971.47 3.21076 1967.01 0 0 1971.49 0.000159692 0.0139498 0.148140 0 0 1971.49 1970.22
Ethylbenzene 0 0 0.484960 139.640 0.196007 139.368 0 0 140.125 0.414935 0.0700250 0.00250295 0 0 140.125 139.564
m-Xylene 0 0 0.295918 99.6939 0.117224 99.5313 0 0 99.9900 0.254442 0.0414765 0.00192758 0 0 99.9900 99.6485
o-Xylene 0 0 0.802055 224.175 0.235466 223.848 0 0 224.977 0.715751 0.0863035 0.00335270 0 0 224.977 224.084
Nonane 0 0 0.00558825 1531.58 0.817559 1530.44 0 0 1531.58 9.99253E-05 0.00548832 0.0341273 0 0 1531.58 1531.26
C10+ 0 0 0.00174540 4342.43 0.226024 4342.12 0 0 4342.44 3.47527E-05 0.00171065 0.00791152 0 0 4342.44 4342.35
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Total Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Property Units
Temperature °F 196.0 70.0 70.0 70.0 75.9 75.9 200.0 300.0 200.0 75.9 75.94 75.9425 75.9425 70 74.4472 70
Pressure psig 200 232 232 232 0 0 300 200 300 0 0 7.86079 232 232 40
Mole Fraction Vapor % 69.7478 100 0 0 100 0 100 0 3.88063 0 100 100 100 0 0.00586936 0
Mole Fraction Light Liquid % 30.2522 0 100 100 0 100 0 100 96.1194 100 0 0 100 1.15245 100
Mole Fraction Heavy Liquid % 0 0 0 0 0 0 0 0 0 0 0 0 0 98.8417 0
Molecular Weight lb/lbmol 19.9 20.9 18.0 98.1 41.5 112.3 20.9 18.0 98.0 18.0 20.0255 41.9378 18.0165 18.9421 106.962
Mass Density lb/ft^3 0.9 1.0 62.3 43.9 0.1 44.8 1.0 57.3 30.2 62.2 0.0513746 0.168514 62.2584 60.4428 44.5615
Molar Flow lbmol/h 33139.4 21959.6 11179.8 130.7 8.7 107.5 21929.6 11209.8 130.8 11175.4 4.39591 0.541542 0 11179.8 11310.6 116.239
Mass Flow lb/h 660018.4 458596.8 201419.7 12823.5 362.0 12071.1 458070.1 201948.3 12825.7 201331.7 88.0302 22.7111 0 201422 214247 12433.1
Vapor Volumetric Flow MCFH 740.7 473.4 3.2 0.3 3.4 0.3 475.4 3.5 0.4 3.2 1.71350 0.134773 3.23525 3.54463 0.279010
Liquid Volumetric Flow Mbbl/d 3166.4 2023.8 13.8 1.2 14.4 1.2 2032.3 15.1 1.8 13.8 7.32448 0.576097 13.8293 15.1518 1.19265
Std Vapor Volumetric Flow MMSCFD 301.8 200.0 101.8 1.2 0.1 1.0 199.7 102.1 1.2 101.8 0.0400363 0.00493216 0 101.822 103.013 1.05866
Std Liquid Volumetric Flow Mbbl/d 105.5 91.6 13.8 1.3 0.1 1.2 91.6 13.8 1.3 13.8 0.0176632 0.00332571 0 13.8178 15.0905 1.20230
Compressibility 0.682 0.936 0.013 0.097 0.985 0.006 0.964 0.008 0.144 0.001 0.996597 0.976633 0.0125593 0.0134879 0.0230970
Specific Gravity 0.721 0.998 0.704 1.433 0.718 0.721 0.920 0.998 0.691426 1.44800 0.998227 0.714482
API Gravity 10.1 68.1 63.6 10.0 10.0 10.0519 65.2156
Enthalpy MMBtu/h -2056.3 -757.9 -1374.8 -11.4 -0.4 -10.3 -723.7 -1332.6 -10.4 -1373.6 -0.161631 -0.0239831 0 -1374.80 -1385.23 -10.7631
Mass Enthalpy Btu/lb -3115.5 -1652.6 -6825.5 -885.1 -1071.8 -851.9 -1579.9 -6598.5 -813.3 -6822.4 -1836.08 -1056.01 -6825.49 -6465.58 -865.683
Mass Cp Btu/(lb*°F) 0.7 0.5 1.0 0.5 0.4 0.5 0.6 1.0 0.6 1.0 0.481124 0.409001 0.983032 0.953614 0.488559
Ideal Gas CpCv Ratio 1.243 1.249 1.326 1.057 1.133 1.049 1.215 1.316 1.046 1.326 1.26077 1.13260 1.32581 1.30847 1.05189
Dynamic Viscosity cP 0.0 1.0 0.4 0.0 0.5 0.0 0.2 0.9 0.0107825 0.00851980 0.995522 0.496561
Kinematic Viscosity cSt 0.7 1.0 0.6 5.0 0.7 0.8 0.2 0.9 13.1023 3.15626 0.998233 0.695651
Thermal Conductivity Btu/(h*ft*°F) 0.0 0.3 0.1 0.0 0.1 0.0 0.4 0.3 0.0173923 0.0107767 0.346442 0.0689748
Surface Tension lbf/ft 0.005 0.001 0.001 0.003 0.005 0.00503944 0.00145907
Net I.G. Heating Value Btu/ft^3 755.6 1140.1 0.5 4954.3 2178.2 5648.8 1141.9 0.0 4950.5 0.0 1052.77 2203.19 0.448229 57.6969 5388.44
Net Liquid Heating Value Btu/lb 14031.1 20654.9 -1049.8 18981.0 19754.5 18916.0 20684.2 -1059.8 18985.5 -1058.9 19868.0 19779.2 -1049.84 149.561 18940.4
Gross I.G. Heating Value Btu/ft^3 850.0 1256.9 50.8 5327.1 2369.3 6067.7 1258.8 50.3 5323.1 50.3 1163.41 2396.10 50.7837 111.759 5790.26
Gross Liquid Heating Value Btu/lb 15829.8 22777.9 10.5 20421.0 21500.6 20330.3 22808.7 0.0 20425.9 0.9 21964.7 21524.7 10.4 1232.5 20364.4
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Vapor Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Mole Fraction % % % % % % % % % % % % % % % %
Water 5.13336 0.157552 0.157689 0.157689 0.229379 0.229379 0 0 3.02994 3.02994 0.000109874 0.157552 0.182990 0.281649
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 0.469285 0.493930 0.548628 0.548628 0.00911088 0.00911088 0.494658 0.224489 0.278296 0.278296 0.000339243 0.493930 0.515935 0.123304
Carbon Dioxide 0.139030 0.145923 0.103900 0.103900 0.122484 0.122484 0.146717 0 0.945391 0.945391 0.130788 0.145923 0.108295 0.168776
Methane 73.7128 77.5798 79.8412 79.8412 11.5107 11.5107 77.7018 58.3535 76.6094 76.6094 2.49734 77.5798 79.0443 50.2902
Ethane 13.4715 14.1779 13.8988 13.8988 34.6571 34.6571 14.2004 22.3546 14.1775 14.1775 43.8560 14.1779 14.3493 30.5508
Propane 4.26379 4.48715 3.58166 3.58166 28.9707 28.9707 4.49433 9.25482 3.85371 3.85371 31.1216 4.48715 3.77925 11.8483
Isobutane 0.537616 0.565850 0.447997 0.447997 5.31811 5.31811 0.566666 1.57691 0.161824 0.161824 5.30483 0.565850 0.478424 1.62199
n-Butane 1.12320 1.18213 0.769918 0.769918 9.96142 9.96142 1.18394 3.07001 0.579212 0.579212 9.76878 1.18213 0.826418 2.83198
Isopentane 0.355720 0.374394 0.210020 0.210020 2.96077 2.96077 0.374944 1.11534 0.103699 0.103699 2.75134 0.374394 0.227999 0.759089
n-Pentane 0.276489 0.291007 0.165308 0.165308 2.38069 2.38069 0.291434 0.981701 0.0794474 0.0794474 2.18589 0.291007 0.180307 0.598147
2-Methylpentane 0 0 0.0603885 0.0603885 0.878065 0.878065 0 0.472998 0.0132459 0.0132459 0.789398 0 0.0665990 0.212222
3-Methylpentane 0 0 0.0292592 0.0292592 0.426199 0.426199 0 0.236740 0.0171318 0.0171318 0.382131 0 0.0323092 0.102684
n-Hexane 0.517220 0.544400 0.0508416 0.0508416 0.735656 0.735656 0.545164 0.447750 0.00876741 0.00876741 0.0448536 0.544400 0.0563469 0.176190
Methylcyclopentane 0 0 0.0103552 0.0103552 0.152715 0.152715 0 0.0898031 0.0178673 0.0178673 0.126811 0 0.0114655 0.0365423
Benzene 0 0 0.00148635 0.00148635 0.0220101 0.0220101 0 0.0134706 0.0168004 0.0168004 0.00113757 0 0.00164406 0.00528803
2-Methylhexane 0 0 0.0199041 0.0199041 0.277903 0.277903 0 0.238108 0.00368683 0.00368683 0.0158226 0 0.0223566 0.0656847
3-Methylhexane 0 0 0.0155017 0.0155017 0.216512 0.216512 0 0.184720 0.00299762 0.00299762 0.185684 0 0.0174020 0.0512034
Heptane 0 0 0.0301303 0.0301303 0.413355 0.413355 0 0.376547 0.00599613 0.00599613 0.326405 0 0.0338657 0.0979494
Methylcyclohexane 0 0 0.0173517 0.0173517 0.244552 0.244552 0 0.208174 0.0187966 0.0187966 0.194948 0 0.0194695 0.0578076
Toluene 0 0 0.00293425 0.00293425 0.0415656 0.0415656 0 0.0378441 0.0298562 0.0298562 0.00453880 0 0.00329813 0.00982322
Octane 0 0 0.0248326 0.0248326 0.322359 0.322359 0 0.446831 0.00277808 0.00277808 0.239478 0 0.0283272 0.0758277
Ethylbenzene 0 0 0.00158175 0.00158175 0.0211736 0.0211736 0 0.0286106 0.0150046 0.0150046 0.00435350 0 0.00180352 0.00496769
m-Xylene 0 0 0.000952294 0.000952294 0.0126632 0.0126632 0 0.0185371 0.00888734 0.00888734 0.00335273 0 0.00108926 0.00296403
o-Xylene 0 0 0.00191269 0.00191269 0.0254362 0.0254362 0 0.0380905 0.0184926 0.0184926 0.00583152 0 0.00218939 0.00595036
Nonane 0 0 0.00590535 0.00590535 0.0731056 0.0731056 0 0.151645 0.000973456 0.000973456 0.0491355 0 0.00683429 0.0169791
C10+ 0 0 0.00148354 0.00148354 0.0162823 0.0162823 0 0.0787916 0.000244438 0.000244438 0.00917666 0 0.00176839 0.00376527
Molar Flow lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h
Water 1186.53 34.5978 0 0 0.0200008 0 0 0 0 0.133193 5.95014E-07 0 0.00121480 0
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 108.471 108.465 0 0 0.000794428 0 108.477 0.0113957 0 0.0122336 1.83714E-06 0 0.00342510 0
Carbon Dioxide 32.1355 32.0442 0 0 0.0106801 0 32.1745 0 0 0.0415585 0.000708274 0 0.000718933 0
Methane 17038.0 17036.2 0 0 1.00368 0 17039.7 2.96218 0 3.36768 0.0135241 0 0.524745 0
Ethane 3113.80 3113.40 0 0 3.02195 0 3114.08 1.13478 0 0.623232 0.237498 0 0.0952598 0
Propane 985.532 985.361 0 0 2.52611 0 985.588 0.469800 0 0.169405 0.168536 0 0.0250890 0
Isobutane 124.265 124.259 0 0 0.463715 0 124.268 0.0800481 0 0.00711361 0.0287279 0 0.00317607 0
n-Butane 259.617 259.592 0 0 0.868591 0 259.633 0.155842 0 0.0254616 0.0529021 0 0.00548627 0
Isopentane 82.2212 82.2154 0 0 0.258166 0 82.2237 0.0566176 0 0.00455853 0.0148997 0 0.00151360 0
n-Pentane 63.9078 63.9040 0 0 0.207586 0 63.9104 0.0498338 0 0.00349243 0.0118375 0 0.00119699 0
2-Methylpentane 0 0 0 0 0.0765633 0 0 0.0240106 0 0.000582276 0.00427492 0 0.000442126 0
3-Methylpentane 0 0 0 0 0.0371627 0 0 0.0120176 0 0.000753098 0.00206940 0 0.000214489 0
n-Hexane 119.550 119.548 0 0 0.0641459 0 119.552 0.0227290 0 0.000385407 0.000242901 0 0.000374066 0
Methylcyclopentane 0 0 0 0 0.0133161 0 0 0.00455865 0 0.000785430 0.000686734 0 7.61148E-05 0
Benzene 0 0 0 0 0.00191918 0 0 0.000683803 0 0.000738531 6.16043E-06 0 1.09143E-05 0
2-Methylhexane 0 0 0 0 0.0242319 0 0 0.0120870 0 0.000162070 8.56861E-05 0 0.000148417 0
3-Methylhexane 0 0 0 0 0.0188789 0 0 0.00937689 0 0.000131772 0.00100556 0 0.000115525 0
Heptane 0 0 0 0 0.0360427 0 0 0.0191145 0 0.000263584 0.00176762 0 0.000224822 0
Methylcyclohexane 0 0 0 0 0.0213238 0 0 0.0105675 0 0.000826280 0.00105572 0 0.000129251 0
Toluene 0 0 0 0 0.00362434 0 0 0.00192107 0 0.00131245 2.45795E-05 0 2.18951E-05 0
Octane 0 0 0 0 0.0281082 0 0 0.0226824 0 0.000122122 0.00129687 0 0.000188054 0
Ethylbenzene 0 0 0 0 0.00184625 0 0 0.00145235 0 0.000659586 2.35760E-05 0 1.19729E-05 0
m-Xylene 0 0 0 0 0.00110417 0 0 0.000940994 0 0.000390679 1.81564E-05 0 7.23119E-06 0
o-Xylene 0 0 0 0 0.00221792 0 0 0.00193358 0 0.000812919 3.15801E-05 0 1.45345E-05 0
Nonane 0 0 0 0 0.00637448 0 0 0.00769794 0 4.27922E-05 0.000266089 0 4.53703E-05 0
C10+ 0 0 0 0 0.00141975 0 0 0.00399967 0 1.07453E-05 4.96955E-05 0 1.17397E-05 0
Mass Fraction % % % % % % % % % % % % % % % %
Water 4.45879 0.135912 0.141807 0.141807 0.0995326 0.0995326 0 0 2.72578 2.72578 4.71987E-05 0.135912 0.162957 0.187408
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 0.633836 0.662560 0.767183 0.767183 0.00614747 0.00614747 0.663391 0.228800 0.389305 0.389305 0.000226605 0.662560 0.714440 0.127580
Carbon Dioxide 0.295006 0.307514 0.228252 0.228252 0.129837 0.129837 0.309119 0 2.07766 2.07766 0.137249 0.307514 0.235592 0.274345
Methane 57.0148 59.5955 63.9371 63.9371 4.44777 4.44777 59.6762 34.0591 61.3719 61.3719 0.955306 59.5955 62.6825 29.7984
Ethane 19.5303 20.4138 20.8618 20.8618 25.1005 25.1005 20.4417 24.4558 21.2881 21.2881 31.4443 20.4138 21.3283 33.9298
Propane 9.06494 9.47457 7.88378 7.88378 30.7698 30.7698 9.48766 14.8477 8.48577 8.48577 32.7228 9.47457 8.23770 19.2970
Isobutane 1.50657 1.57484 1.29978 1.29978 7.44509 7.44509 1.57677 3.33460 0.469678 0.469678 7.35203 1.57484 1.37455 3.48201
n-Butane 3.14756 3.29005 2.23378 2.23378 13.9455 13.9455 3.29435 6.49199 1.68111 1.68111 13.5387 3.29005 2.37436 6.07955
Isopentane 1.23740 1.29345 0.756387 0.756387 5.14522 5.14522 1.29507 2.92773 0.373613 0.373613 4.73333 1.29345 0.813144 2.02284
n-Pentane 0.961792 1.00537 0.595358 0.595358 4.13717 4.13717 1.00663 2.57694 0.286237 0.286237 3.76055 1.00537 0.643052 1.59396
2-Methylpentane 0 0 0.259772 0.259772 1.82255 1.82255 0 1.48299 0.0570007 0.0570007 1.62208 0 0.283697 0.675479
3-Methylpentane 0 0 0.125864 0.125864 0.884640 0.884640 0 0.742251 0.0737230 0.0737230 0.785217 0 0.137630 0.326831
n-Hexane 2.14898 2.24644 0.218704 0.218704 1.52696 1.52696 2.24910 1.40383 0.0377287 0.0377287 0.0921668 2.24644 0.240026 0.560795
Methylcyclopentane 0 0 0.0435025 0.0435025 0.309568 0.309568 0 0.274973 0.0750894 0.0750894 0.254480 0 0.0476979 0.113589
Benzene 0 0 0.00579552 0.00579552 0.0414104 0.0414104 0 0.0382823 0.0655321 0.0655321 0.00211880 0 0.00634805 0.0152563
2-Methylhexane 0 0 0.0995573 0.0995573 0.670718 0.670718 0 0.868053 0.0184479 0.0184479 0.0378049 0 0.110735 0.243097
3-Methylhexane 0 0 0.0775372 0.0775372 0.522552 0.522552 0 0.673419 0.0149992 0.0149992 0.443654 0 0.0861946 0.189502
Heptane 0 0 0.150708 0.150708 0.997631 0.997631 0 1.37275 0.0300029 0.0300029 0.779877 0 0.167742 0.362508
Methylcyclohexane 0 0 0.0850446 0.0850446 0.578351 0.578351 0 0.743657 0.0921606 0.0921606 0.456417 0 0.0944952 0.209640
Toluene 0 0 0.0134956 0.0134956 0.0922456 0.0922456 0 0.126863 0.137370 0.137370 0.00997185 0 0.0150215 0.0334298
Octane 0 0 0.141596 0.141596 0.886920 0.886920 0 1.85701 0.0158466 0.0158466 0.652279 0 0.159950 0.319920
Ethylbenzene 0 0 0.00838248 0.00838248 0.0541436 0.0541436 0 0.110511 0.0795465 0.0795465 0.0110208 0 0.00946468 0.0194794
m-Xylene 0 0 0.00504670 0.00504670 0.0323813 0.0323813 0 0.0716010 0.0471162 0.0471162 0.00848737 0 0.00571634 0.0116226
o-Xylene 0 0 0.0101363 0.0101363 0.0650436 0.0650436 0 0.147128 0.0980385 0.0980385 0.0147624 0 0.0114897 0.0233327
Nonane 0 0 0.0378072 0.0378072 0.225837 0.225837 0 0.707620 0.00623459 0.00623459 0.150267 0 0.0433284 0.0804321
C10+ 0 0 0.0117896 0.0117896 0.0624354 0.0624354 0 0.456371 0.00194325 0.00194325 0.0348355 0 0.0139164 0.0221401
Mass Flow lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h
Water 21375.6 623.289 0 0 0.360321 0 0 0 0 2.39951 1.07193E-05 0 0.0218850 0
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 3038.63 3038.48 0 0 0.0222546 0 3038.80 0.319232 0 0.342706 5.14646E-05 0 0.0959487 0
Carbon Dioxide 1414.27 1410.25 0 0 0.470025 0 1415.98 0 0 1.82897 0.0311708 0 0.0316399 0
Methane 273331 273303 0 0 16.1015 0 273359 47.5207 0 54.0258 0.216960 0 8.41820 0
Ethane 93629.0 93617.1 0 0 90.8670 0 93637.5 34.1217 0 18.7400 7.14135 0 2.86437 0
Propane 43457.7 43450.1 0 0 111.391 0 43460.1 20.7161 0 7.47004 7.43172 0 1.10632 0
Isobutane 7222.53 7222.18 0 0 26.9522 0 7222.71 4.65257 0 0.413459 1.66973 0 0.184600 0
n-Butane 15089.5 15088.1 0 0 50.4844 0 15090.4 9.05788 0 1.47988 3.07478 0 0.318874 0
Isopentane 5932.16 5931.74 0 0 18.6263 0 5932.34 4.08489 0 0.328892 1.07499 0 0.109205 0
n-Pentane 4610.87 4610.60 0 0 14.9771 0 4611.05 3.59545 0 0.251975 0.854062 0 0.0863613 0
2-Methylpentane 0 0 0 0 6.59787 0 0 2.06913 0 0.0501778 0.368393 0 0.0381003 0
3-Methylpentane 0 0 0 0 3.20251 0 0 1.03562 0 0.0648985 0.178331 0 0.0184837 0
n-Hexane 10302.3 10302.1 0 0 5.52779 0 10302.5 1.95868 0 0.0332126 0.0209321 0 0.0322352 0
Methylcyclopentane 0 0 0 0 1.12067 0 0 0.383654 0 0.0661014 0.0577952 0 0.00640578 0
Benzene 0 0 0 0 0.149911 0 0 0.0534131 0 0.0576880 0.000481203 0 0.000852538 0
2-Methylhexane 0 0 0 0 2.42808 0 0 1.21114 0 0.0162397 0.00858592 0 0.0148717 0
3-Methylhexane 0 0 0 0 1.89170 0 0 0.939582 0 0.0132038 0.100759 0 0.0115759 0
Heptane 0 0 0 0 3.61155 0 0 1.91531 0 0.0264117 0.177119 0 0.0225276 0
Methylcyclohexane 0 0 0 0 2.09370 0 0 1.03758 0 0.0811291 0.103657 0 0.0126906 0
Toluene 0 0 0 0 0.333941 0 0 0.177004 0 0.120927 0.00226472 0 0.00201738 0
Octane 0 0 0 0 3.21076 0 0 2.59097 0 0.0139498 0.148140 0 0.0214811 0
Ethylbenzene 0 0 0 0 0.196007 0 0 0.154189 0 0.0700250 0.00250295 0 0.00127110 0
m-Xylene 0 0 0 0 0.117224 0 0 0.0999006 0 0.0414765 0.00192758 0 0.000767700 0
o-Xylene 0 0 0 0 0.235466 0 0 0.205278 0 0.0863035 0.00335270 0 0.00154306 0
Nonane 0 0 0 0 0.817559 0 0 0.987300 0 0.00548832 0.0341273 0 0.00581897 0
C10+ 0 0 0 0 0.226024 0 0 0.636748 0 0.00171065 0.00791152 0 0.00186896 0
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Vapor Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Property Units
Temperature °F 196.0 70.0 70.0 70.0 75.9 75.9 200.0 200.0 75.9 75.94 75.9425 70 74.4472 70
Pressure psig 200 232 232 232 0 0 300 300 0 0 7.86079 232 232 40
Mole Fraction Vapor % 100 100 100 100 100 100 100 100 100 100 100 100 100 100
Mole Fraction Light Liquid % 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Mole Fraction Heavy Liquid % 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Molecular Weight lb/lbmol 20.7 20.9 20.0 20.0 41.5 41.5 20.9 27.5 20.0 20.0255 41.9378 20.8836 20.2300 27.0745
Mass Density lb/ft^3 0.6 1.0 0.9 0.9 0.1 0.1 1.0 1.3 0.1 0.0513746 0.168514 0.968639 0.924813 0.267108
Molar Flow lbmol/h 23114.0 21959.6 0.0 0.0 8.7 0.0 21929.6 5.1 0.0 4.39591 0.541542 0 0.663862 0
Mass Flow lb/h 479403.8 458596.8 0.0 0.0 362.0 0.0 458070.1 139.5 0.0 88.0302 22.7111 0 13.4299 0
Vapor Volumetric Flow MCFH 737.7 473.4 0.0 0.0 3.4 0.0 475.4 0.1 0.0 1.71350 0.134773 0 0.0145218 0
Liquid Volumetric Flow Mbbl/d 3153.5 2023.8 0.0 0.0 14.4 0.0 2032.3 0.5 0.0 7.32448 0.576097 0 0.0620745 0
Std Vapor Volumetric Flow MMSCFD 210.5 200.0 0.0 0.0 0.1 0.0 199.7 0.0 0.0 0.0400363 0.00493216 0 0.00604621 0
Std Liquid Volumetric Flow Mbbl/d 93.1 91.6 0.0 0.0 0.1 0.0 91.6 0.0 0.0 0.0176632 0.00332571 0 0.00273728 0
Compressibility 0.974 0.936 0.941 0.941 0.985 0.985 0.964 0.931 0.997 0.996597 0.976633 0.935701 0.941462 0.975346
Specific Gravity 0.716 0.721 0.692 0.692 1.433 1.433 0.721 0.949 0.691 0.691426 1.44800 0.721056 0.698486 0.934809
API Gravity
Enthalpy MMBtu/h -845.7 -757.9 0.0 0.0 -0.4 0.0 -723.7 -0.2 0.0 -0.161631 -0.0239831 0 -0.0226063 0
Mass Enthalpy Btu/lb -1764.0 -1652.6 -1695.8 -1695.8 -1071.8 -1071.8 -1579.9 -1305.5 -1836.1 -1836.08 -1056.01 -1652.59 -1683.28 -1376.04
Mass Cp Btu/(lb*°F) 0.5 0.5 0.5 0.5 0.4 0.4 0.6 0.5 0.5 0.481124 0.409001 0.511047 0.515331 0.448184
Ideal Gas CpCv Ratio 1.220 1.249 1.258 1.258 1.133 1.133 1.215 1.165 1.261 1.26077 1.13260 1.24907 1.25517 1.20007
Dynamic Viscosity cP 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0107825 0.00851980 0.0108061 0.0109382 0.00979749
Kinematic Viscosity cSt 1.2 0.7 0.7 0.7 5.0 5.0 0.8 0.6 13.1 13.1023 3.15626 0.696444 0.738367 2.28985
Thermal Conductivity Btu/(h*ft*°F) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0173923 0.0107767 0.0178833 0.0182457 0.0147553
Surface Tension lbf/ft
Net I.G. Heating Value Btu/ft^3 1083.3 1140.1 1097.7 1097.7 2178.2 2178.2 1141.9 1478.1 1052.8 1052.77 2203.19 1140.11 1107.68 1454.42
Net Liquid Heating Value Btu/lb 19714.7 20654.9 20737.1 20737.1 19754.5 19754.5 20684.2 20299.7 19868.0 19868.0 19779.2 20654.9 20720.0 20273.8
Gross I.G. Heating Value Btu/ft^3 1196.8 1256.9 1211.4 1211.4 2369.3 2369.3 1258.8 1619.0 1163.4 1163.41 2396.10 1256.94 1222.17 1593.74
Gross Liquid Heating Value Btu/lb 21791.7 22777.9 22892.1 22892.1 21500.6 21500.6 22808.7 22243.9 21964.7 21964.7 21524.7 22777.9 22867.6 22226.5
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Light Liquid Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Mole Fraction % % % % % % % % % % % % % % % %
Water 99.9789 99.9589 99.9588 0.0501987 0.00462880 0.00462880 100 0 99.9969 99.9969 3.09946E-06 99.9589 0.0564055 0.0214883
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 5.85400E-05 0.000101795 0.000112685 0.0142266 1.35784E-05 1.35784E-05 0 0.00758266 3.26005E-06 3.26005E-06 8.05777E-07 0.000101795 0.0133286 0.000696006
Carbon Dioxide 0.000388856 0.00116544 0.000829929 0.0285456 0.00212169 0.00212169 0 0 0.000458380 0.000458380 0.00338399 0.00116544 0.0287796 0.0111506
Methane 0.0170314 0.0310988 0.0319662 6.36327 0.0549825 0.0549825 0 4.46374 0.00184397 0.00184397 0.0187897 0.0310988 6.20443 0.914323
Ethane 0.00283744 0.00607361 0.00597218 6.55557 1.05871 1.05871 0 5.92336 0.000397706 0.000397706 2.07549 0.00607361 6.52335 3.57907
Propane 0.000557248 0.00203453 0.00163468 5.98557 3.33530 3.33530 0 5.81657 0.000119446 0.000119446 5.50989 0.00203453 5.98821 5.25832
Isobutane 3.07495E-05 8.17882E-05 6.53738E-05 1.82784 1.57239 1.57239 0 1.83502 1.74525E-06 1.74525E-06 2.37939 8.17882E-05 1.83039 1.85337
n-Butane 0.000162735 0.000367047 0.000241498 4.46074 4.23308 4.23308 0 4.50155 1.37563E-05 1.37563E-05 6.29140 0.000367047 4.46782 4.66279
Isopentane 2.53167E-05 7.47499E-05 4.24621E-05 2.96090 3.25618 3.25618 0 3.02927 1.68795E-06 1.68795E-06 4.56963 7.47499E-05 2.96701 3.23402
n-Pentane 2.58072E-05 5.64763E-05 3.25188E-05 3.11443 3.51139 3.51139 0 3.19489 1.28046E-06 1.28046E-06 4.85687 5.64763E-05 3.12104 3.42657
2-Methylpentane 0 0 5.30992E-06 2.68359 3.16144 3.16144 0 2.77014 1.01661E-07 1.01661E-07 4.27791 0 2.68967 2.99016
3-Methylpentane 0 0 7.09285E-06 1.44904 1.71255 1.71255 0 1.49690 3.56740E-07 3.56740E-07 2.30742 0 1.45233 1.61605
n-Hexane 1.92384E-05 3.68296E-05 3.50085E-06 3.10340 3.68797 3.68797 0 3.20396 5.35076E-08 5.35076E-08 0.337708 3.68296E-05 3.11052 3.46651
Methylcyclopentane 0 0 8.14194E-06 0.667069 0.793339 0.793339 0 0.690303 1.11693E-06 1.11693E-06 0.982869 0 0.668604 0.745283
Benzene 0 0 5.89487E-05 0.0970732 0.115470 0.115470 0 0.105574 5.23633E-05 5.23633E-05 0.00872975 0 0.0972302 0.108459
2-Methylhexane 0 0 1.47359E-06 2.71802 3.27161 3.27161 0 2.81500 2.39339E-08 2.39339E-08 0.276638 0 2.72437 3.04704
3-Methylhexane 0 0 1.19900E-06 2.22348 2.67755 2.67755 0 2.30321 2.03400E-08 2.03400E-08 3.40629 0 2.22867 2.49294
Heptane 0 0 2.39859E-06 5.34300 6.44617 6.44617 0 5.53727 4.09139E-08 4.09139E-08 7.52717 0 5.35552 5.99363
Methylcyclohexane 0 0 8.16811E-06 3.13194 3.77836 3.77836 0 3.24692 7.77571E-07 7.77571E-07 4.45233 0 3.13926 3.51327
Toluene 0 0 8.86372E-05 0.655187 0.791497 0.791497 0 0.687199 7.69279E-05 7.69279E-05 0.127275 0 0.656492 0.735241
Octane 0 0 1.10485E-06 13.2093 16.0157 16.0157 0 13.7086 1.25097E-08 1.25097E-08 17.4932 0 13.2405 14.8385
Ethylbenzene 0 0 4.08593E-05 1.00668 1.22094 1.22094 0 1.04858 3.49733E-05 3.49733E-05 0.367056 0 1.00899 1.13094
m-Xylene 0 0 2.49320E-05 0.718709 0.871953 0.871953 0 0.748320 2.14459E-05 2.14459E-05 0.337292 0 0.720337 0.807494
o-Xylene 0 0 6.75755E-05 1.61611 1.96105 1.96105 0 1.68387 6.03279E-05 6.03279E-05 0.655596 0 1.61972 1.81585
Nonane 0 0 3.89733E-07 9.13965 11.0983 11.0983 0 9.49144 6.97170E-09 6.97170E-09 11.0431 0 9.16125 10.2713
C10+ 0 0 9.80662E-08 20.8764 25.3673 25.3673 0 21.6907 1.95336E-09 1.95336E-09 20.6945 0 20.9258 23.4656
Molar Flow lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h
Water 10023.3 0 11175.2 0.0655883 0 0.00497684 11209.8 0 11175.0 0 0 11175.2 0.0735240 0.0249777
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 0.00586888 0 0.0125980 0.0185881 0 1.45994E-05 0 0.00953401 0.000364323 0 0 0.0113805 0.0173738 0.000809027
Carbon Dioxide 0.0389845 0 0.0927842 0.0372970 0 0.00228122 0 0 0.0512257 0 0 0.130294 0.0375139 0.0129613
Methane 1.70747 0 3.57375 8.31409 0 0.0591167 0 5.61245 0.206071 0 0 3.47679 8.08741 1.06280
Ethane 0.284465 0 0.667677 8.56534 0 1.13831 0 7.44770 0.0444452 0 0 0.679019 8.50312 4.16026
Propane 0.0558665 0 0.182754 7.82059 0 3.58608 0 7.31343 0.0133485 0 0 0.227457 7.80557 6.11220
Isobutane 0.00308276 0 0.00730865 2.38821 0 1.69062 0 2.30724 0.000195038 0 0 0.00914378 2.38589 2.15434
n-Butane 0.0163149 0 0.0269989 5.82829 0 4.55136 0 5.65999 0.00153732 0 0 0.0410352 5.82376 5.41995
Isopentane 0.00253811 0 0.00474716 3.86863 0 3.50101 0 3.80883 0.000188635 0 0 0.00835691 3.86746 3.75918
n-Pentane 0.00258728 0 0.00363553 4.06924 0 3.77541 0 4.01707 0.000143096 0 0 0.00631396 4.06825 3.98299
2-Methylpentane 0 0 0.000593637 3.50631 0 3.39915 0 3.48302 1.13611E-05 0 0 0 3.50596 3.47571
3-Methylpentane 0 0 0.000792965 1.89328 0 1.84131 0 1.88212 3.98670E-05 0 0 0 1.89310 1.87848
n-Hexane 0.00192873 0 0.000391387 4.05482 0 3.96527 0 4.02847 5.97968E-06 0 0 0.00411749 4.05453 4.02942
Methylcyclopentane 0 0 0.000910250 0.871575 0 0.852990 0 0.867948 0.000124821 0 0 0 0.871519 0.866306
Benzene 0 0 0.00659033 0.126833 0 0.124152 0 0.132743 0.00585180 0 0 0 0.126739 0.126071
2-Methylhexane 0 0 0.000164744 3.55130 0 3.51760 0 3.53942 2.67471E-06 0 0 0 3.55119 3.54183
3-Methylhexane 0 0 0.000134045 2.90514 0 2.87887 0 2.89592 2.27307E-06 0 0 0 2.90505 2.89775
Heptane 0 0 0.000268157 6.98103 0 6.93086 0 6.96224 4.57228E-06 0 0 0 6.98087 6.96690
Methylcyclohexane 0 0 0.000913176 4.09211 0 4.06245 0 4.08249 8.68966E-05 0 0 0 4.09199 4.08378
Toluene 0 0 0.00990944 0.856050 0 0.851009 0 0.864045 0.00859699 0 0 0 0.855730 0.854634
Octane 0 0 0.000123520 17.2590 0 17.2199 0 17.2365 1.39801E-06 0 0 0 17.2588 17.2480
Ethylbenzene 0 0 0.00456798 1.31531 0 1.31274 0 1.31843 0.00390840 0 0 0 1.31520 1.31459
m-Xylene 0 0 0.00278734 0.939046 0 0.937515 0 0.940895 0.00239666 0 0 0 0.938952 0.938619
o-Xylene 0 0 0.00755479 2.11157 0 2.10850 0 2.11720 0.00674187 0 0 0 2.11128 2.11071
Nonane 0 0 4.35713E-05 11.9416 0 11.9328 0 11.9340 7.79114E-07 0 0 0 11.9416 11.9392
C10+ 0 0 1.09636E-05 27.2766 0 27.2746 0 27.2726 2.18296E-07 0 0 0 27.2766 27.2761
Mass Fraction % % % % % % % % % % % % % % % %
Water 99.9768 99.9520 99.9524 0.00921427 0.000742758 0.000742758 100 0 99.9949 99.9949 5.26991E-07 99.9520 0.0103346 0.00361920
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 9.10266E-05 0.000158278 0.000175212 0.00406065 3.38807E-06 3.38807E-06 0 0.00210528 5.06921E-06 5.06921E-06 2.13038E-07 0.000158278 0.00379739 0.000182284
Carbon Dioxide 0.000949916 0.00284685 0.00202730 0.0128001 0.000831699 0.000831699 0 0 0.00111975 0.00111975 0.00140557 0.00284685 0.0128814 0.00458791
Methane 0.0151660 0.0276913 0.0284638 1.04011 0.00785659 0.00785659 0 0.709728 0.00164201 0.00164201 0.00284490 0.0276913 1.01229 0.137133
Ethane 0.00473582 0.0101367 0.00996744 2.00843 0.283553 0.283553 0 1.76527 0.000663792 0.000663792 0.589003 0.0101367 1.99491 1.00614
Propane 0.00136393 0.00497952 0.00400092 2.68923 1.30999 1.30999 0 2.54205 0.000292359 0.000292359 2.29305 0.00497952 2.68550 2.16777
Isobutane 9.92041E-05 0.000263853 0.000210900 1.08245 0.814031 0.814031 0 1.05707 5.63053E-06 5.63053E-06 1.30522 0.000263853 1.08198 1.00711
n-Butane 0.000525018 0.00118411 0.000779088 2.64166 2.19148 2.19148 0 2.59314 4.43808E-05 4.43808E-05 3.45116 0.00118411 2.64101 2.53371
Isopentane 0.000101388 0.000299343 0.000170044 2.17660 2.09255 2.09255 0 2.16615 6.75989E-06 6.75989E-06 3.11162 0.000299343 2.17711 2.18143
n-Pentane 0.000103352 0.000226165 0.000130225 2.28947 2.25655 2.25655 0 2.28458 5.12795E-06 5.12795E-06 3.30721 0.000226165 2.29014 2.31131
2-Methylpentane 0 0 2.53981E-05 2.35628 2.42665 2.42665 0 2.36596 4.86284E-07 4.86284E-07 3.47930 0 2.35730 2.40906
3-Methylpentane 0 0 3.39262E-05 1.27231 1.31451 1.31451 0 1.27849 1.70641E-06 1.70641E-06 1.87666 0 1.27286 1.30199
n-Hexane 9.20240E-05 0.000176161 1.67451E-05 2.72489 2.83080 2.83080 0 2.73648 2.55946E-07 2.55946E-07 0.274663 0.000176161 2.72615 2.79284
Methylcyclopentane 0 0 3.80331E-05 0.572007 0.594703 0.594703 0 0.575791 5.21768E-06 5.21768E-06 0.780683 0 0.572275 0.586400
Benzene 0 0 0.000255577 0.0772580 0.0803383 0.0803383 0 0.0817329 0.000227036 0.000227036 0.00643569 0 0.0772415 0.0792048
2-Methylhexane 0 0 8.19567E-06 2.77496 2.91995 2.91995 0 2.79561 1.33119E-07 1.33119E-07 0.261616 0 2.77636 2.85446
3-Methylhexane 0 0 6.66847E-06 2.27005 2.38975 2.38975 0 2.28735 1.13130E-07 1.13130E-07 3.22132 0 2.27120 2.33538
Heptane 0 0 1.33402E-05 5.45493 5.75329 5.75329 0 5.49913 2.27561E-07 2.27561E-07 7.11842 0 5.45771 5.61482
Methylcyclohexane 0 0 4.45146E-05 3.13322 3.30439 3.30439 0 3.15969 4.23780E-06 4.23780E-06 4.12585 0 3.13480 3.22502
Toluene 0 0 0.000453302 0.615083 0.649573 0.649573 0 0.627546 0.000393437 0.000393437 0.110678 0 0.615181 0.633346
Octane 0 0 7.00501E-06 15.3739 16.2952 16.2952 0 15.5200 7.93179E-08 7.93179E-08 18.8591 0 15.3819 15.8465
Ethylbenzene 0 0 0.000240771 1.08893 1.15455 1.15455 0 1.10333 0.000206095 0.000206095 0.367782 0 1.08943 1.12251
m-Xylene 0 0 0.000146916 0.777431 0.824542 0.824542 0 0.787392 0.000126379 0.000126379 0.337959 0 0.777767 0.801476
o-Xylene 0 0 0.000398201 1.74816 1.85442 1.85442 0 1.77179 0.000355508 0.000355508 0.656891 0 1.74885 1.80232
Nonane 0 0 2.77443E-06 11.9435 12.6786 12.6786 0 12.0650 4.96322E-08 4.96322E-08 13.3672 0 11.9498 12.3160
C10+ 0 0 8.66550E-07 33.8631 35.9712 35.9712 0 34.2246 1.72614E-08 1.72614E-08 31.0939 0 33.8812 34.9257
Mass Flow lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h
Water 180573 0 201324 1.18159 0 0.0896591 201948 0 201321 0 0 201325 1.32456 0.449980
H2S 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Nitrogen 0.164407 0 0.352912 0.520717 0 0.000408978 0 0.267080 0.0102059 0 0 0.318807 0.486698 0.0226636
Carbon Dioxide 1.71569 0 4.08339 1.64142 0 0.100395 0 0 2.25442 0 0 5.73418 1.65097 0.570420
Methane 27.3921 0 57.3317 133.378 0 0.948377 0 90.0375 3.30589 0 0 55.7763 129.742 17.0499
Ethane 8.55359 0 20.0764 257.552 0 34.2279 0 223.945 1.33642 0 0 20.4174 255.681 125.095
Propane 2.46347 0 8.05865 344.854 0 158.130 0 322.490 0.588612 0 0 10.0298 344.191 269.521
Isobutane 0.179177 0 0.424795 138.808 0 98.2626 0 134.102 0.0113360 0 0 0.531456 138.673 125.215
n-Butane 0.948259 0 1.56924 338.753 0 264.535 0 328.971 0.0893526 0 0 2.38506 338.490 315.020
Isopentane 0.183122 0 0.342502 279.117 0 252.594 0 274.803 0.0136098 0 0 0.602941 279.033 271.220
n-Pentane 0.186669 0 0.262299 293.591 0 272.391 0 289.826 0.0103242 0 0 0.455544 293.519 287.368
2-Methylpentane 0 0 0.0511569 302.158 0 292.923 0 300.150 0.000979043 0 0 0 302.128 299.521
3-Methylpentane 0 0 0.0683341 163.154 0 158.676 0 162.192 0.00343555 0 0 0 163.138 161.878
n-Hexane 0.166209 0 0.0337279 349.426 0 341.709 0 347.155 0.000515301 0 0 0.354826 349.401 347.237
Methylcyclopentane 0 0 0.0766062 73.3513 0 71.7872 0 73.0460 0.0105048 0 0 0 73.3466 72.9078
Benzene 0 0 0.514783 9.90719 0 9.69772 0 10.3688 0.457095 0 0 0 9.89978 9.84763
2-Methylhexane 0 0 0.0165077 355.847 0 352.470 0 354.657 0.000268011 0 0 0 355.836 354.898
3-Methylhexane 0 0 0.0134316 291.100 0 288.469 0 290.177 0.000227766 0 0 0 291.092 290.360
Heptane 0 0 0.0268698 699.513 0 694.486 0 697.630 0.000458152 0 0 0 699.497 698.097
Methylcyclohexane 0 0 0.0896612 401.788 0 398.876 0 400.844 0.00853203 0 0 0 401.776 400.970
Toluene 0 0 0.913040 78.8751 0 78.4107 0 79.6117 0.792113 0 0 0 78.8457 78.7446
Octane 0 0 0.0141095 1971.47 0 1967.01 0 1968.90 0.000159692 0 0 0 1971.45 1970.22
Ethylbenzene 0 0 0.484960 139.640 0 139.368 0 139.971 0.414935 0 0 0 139.628 139.564
m-Xylene 0 0 0.295918 99.6939 0 99.5313 0 99.8901 0.254442 0 0 0 99.6838 99.6485
o-Xylene 0 0 0.802055 224.175 0 223.848 0 224.772 0.715751 0 0 0 224.144 224.084
Nonane 0 0 0.00558825 1531.58 0 1530.44 0 1530.60 9.99253E-05 0 0 0 1531.57 1531.26
C10+ 0 0 0.00174540 4342.43 0 4342.12 0 4341.80 3.47527E-05 0 0 0 4342.43 4342.35
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Light Liquid Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Property Units
Temperature °F 196.0 70.0 70.0 70.0 75.9 75.9 300.0 200.0 75.9 75.94 75.9425 70 74.4472 70
Pressure psig 200 232 232 232 0 0 200 300 0 0 7.86079 232 232 40
Mole Fraction Vapor % 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Mole Fraction Light Liquid % 100 100 100 100 100 100 100 100 100 100 100 100 100 100
Mole Fraction Heavy Liquid % 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Molecular Weight lb/lbmol 18.0 18.0 18.0 98.1 112.3 112.3 18.0 100.9 18.0 18.0156 105.956 18.0165 98.3257 106.962
Mass Density lb/ft^3 60.2 62.3 62.3 43.9 44.8 44.8 57.3 39.9 62.2 62.2170 43.9457 62.2584 43.7805 44.5615
Molar Flow lbmol/h 10025.4 0.0 11179.8 130.7 0.0 107.5 11209.8 125.7 11175.4 0 0 11179.8 130.349 116.239
Mass Flow lb/h 180614.6 0.0 201419.7 12823.5 0.0 12071.1 201948.3 12686.2 201331.7 0 0 201422 12816.7 12433.1
Vapor Volumetric Flow MCFH 3.0 0.0 3.2 0.3 0.0 0.3 3.5 0.3 3.2 0 0 3.23525 0.292748 0.279010
Liquid Volumetric Flow Mbbl/d 12.8 0.0 13.8 1.2 0.0 1.2 15.1 1.4 13.8 0 0 13.8293 1.25138 1.19265
Std Vapor Volumetric Flow MMSCFD 91.3 0.0 101.8 1.2 0.0 1.0 102.1 1.1 101.8 0 0 101.822 1.18717 1.05866
Std Liquid Volumetric Flow Mbbl/d 12.4 0.0 13.8 1.3 0.0 1.2 13.8 1.2 13.8 0 0 13.8178 1.27060 1.20230
Compressibility 0.009 0.013 0.013 0.097 0.006 0.006 0.008 0.112 0.001 0.000740330 0.00946170 0.0125593 0.0966602 0.0230970
Specific Gravity 0.966 0.998 0.998 0.704 0.718 0.718 0.920 0.640 0.998 0.997563 0.704607 0.998227 0.701959 0.714482
API Gravity 10.0 10.1 10.1 68.1 63.6 63.6 10.0 66.8 10.0 10.0154 67.1452 10.0519 67.9990 65.2156
Enthalpy MMBtu/h -1210.6 0.0 -1374.8 -11.4 0.0 -10.3 -1332.6 -10.2 -1373.6 0 0 -1374.80 -11.3115 -10.7631
Mass Enthalpy Btu/lb -6702.7 -6825.5 -6825.5 -885.1 -851.9 -851.9 -6598.5 -807.9 -6822.4 -6822.37 -894.385 -6825.49 -882.565 -865.683
Mass Cp Btu/(lb*°F) 1.0 1.0 1.0 0.5 0.5 0.5 1.0 0.6 1.0 0.982733 0.495520 0.983032 0.496970 0.488559
Ideal Gas CpCv Ratio 1.320 1.326 1.326 1.057 1.049 1.049 1.316 1.045 1.326 1.32555 1.05147 1.32581 1.05599 1.05189
Dynamic Viscosity cP 0.3 1.0 1.0 0.4 0.5 0.5 0.2 0.2 0.9 0.924439 0.464685 0.995522 0.412845 0.496561
Kinematic Viscosity cSt 0.3 1.0 1.0 0.6 0.7 0.7 0.2 0.4 0.9 0.927573 0.660118 0.998233 0.588688 0.695651
Thermal Conductivity Btu/(h*ft*°F) 0.4 0.3 0.3 0.1 0.1 0.1 0.4 0.1 0.3 0.349783 0.0684782 0.346442 0.0679228 0.0689748
Surface Tension lbf/ft 0.004 0.005 0.005 0.001 0.001 0.001 0.003 0.001 0.005 0.00499713 0.00142196 0.00503944 0.00128518 0.00145907
Net I.G. Heating Value Btu/ft^3 0.2 0.4 0.5 4954.3 5648.8 5648.8 0.0 5090.7 0.0 0.0376228 5353.06 0.448229 4963.09 5388.44
Net Liquid Heating Value Btu/lb -1054.8 -1049.8 -1049.8 18981.0 18916.0 18916.0 -1059.8 18971.1 -1058.9 -1058.92 19002.0 -1049.84 18979.8 18940.4
Gross I.G. Heating Value Btu/ft^3 50.5 50.8 50.8 5327.1 6067.7 6067.7 50.3 5472.6 50.3 50.3493 5757.94 50.7837 5336.53 5790.26
Gross Liquid Heating Value Btu/lb 5.2 10.4 10.5 20421.0 20330.3 20330.3 0.0 20406.0 0.9 0.856779 20451.0 10.3851 20419.5 20364.4
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Heavy Liquid Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Mole Fraction % % % % % % % % % % % % % % % %
Water 99.9588 99.9600
H2S 0 0
Nitrogen 0.000112685 0.000102967
Carbon Dioxide 0.000829929 0.000823473
Methane 0.0319662 0.0307637
Ethane 0.00597218 0.00593152
Propane 0.00163468 0.00161029
Isobutane 6.53738E-05 6.59153E-05
n-Butane 0.000241498 0.000247087
Isopentane 4.24621E-05 4.32177E-05
n-Pentane 3.25188E-05 3.37314E-05
2-Methylpentane 5.30992E-06 5.59628E-06
3-Methylpentane 7.09285E-06 7.39150E-06
n-Hexane 3.50085E-06 3.69537E-06
Methylcyclopentane 8.14194E-06 8.14905E-06
Benzene 5.89487E-05 5.97267E-05
2-Methylhexane 1.47359E-06 1.48986E-06
3-Methylhexane 1.19900E-06 1.21512E-06
Heptane 2.39859E-06 2.35359E-06
Methylcyclohexane 8.16811E-06 8.45018E-06
Toluene 8.86372E-05 9.13564E-05
Octane 1.10485E-06 1.17734E-06
Ethylbenzene 4.08593E-05 4.17166E-05
m-Xylene 2.49320E-05 2.57348E-05
o-Xylene 6.75755E-05 7.00662E-05
Nonane 3.89733E-07 4.15654E-07
C10+ 9.80662E-08 1.05052E-07
Molar Flow lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h lbmol/h
Water 0 11175.2
H2S 0 0
Nitrogen 0 0.0115113
Carbon Dioxide 0 0.0920612
Methane 0 3.43926
Ethane 0 0.663122
Propane 0 0.180024
Isobutane 0 0.00736909
n-Butane 0 0.0276234
Isopentane 0 0.00483158
n-Pentane 0 0.00377104
2-Methylpentane 0 0.000625643
3-Methylpentane 0 0.000826342
n-Hexane 0 0.000413129
Methylcyclopentane 0 0.000911033
Benzene 0 0.00667723
2-Methylhexane 0 0.000166561
3-Methylhexane 0 0.000135845
Heptane 0 0.000263123
Methylcyclohexane 0 0.000944699
Toluene 0 0.0102133
Octane 0 0.000131623
Ethylbenzene 0 0.00466376
m-Xylene 0 0.00287705
o-Xylene 0 0.00783314
Nonane 0 4.64686E-05
C10+ 0 1.17444E-05
Mass Fraction % % % % % % % % % % % % % % % %
Water 99.9524 99.9535
H2S 0 0
Nitrogen 0.000175212 0.000160101
Carbon Dioxide 0.00202730 0.00201153
Methane 0.0284638 0.0273930
Ethane 0.00996744 0.00989956
Propane 0.00400092 0.00394121
Isobutane 0.000210900 0.000212647
n-Butane 0.000779088 0.000797118
Isopentane 0.000170044 0.000173070
n-Pentane 0.000130225 0.000135081
2-Methylpentane 2.53981E-05 2.67678E-05
3-Methylpentane 3.39262E-05 3.53546E-05
n-Hexane 1.67451E-05 1.76755E-05
Methylcyclopentane 3.80331E-05 3.80663E-05
Benzene 0.000255577 0.000258950
2-Methylhexane 8.19567E-06 8.28614E-06
3-Methylhexane 6.66847E-06 6.75810E-06
Heptane 1.33402E-05 1.30900E-05
Methylcyclohexane 4.45146E-05 4.60518E-05
Toluene 0.000453302 0.000467208
Octane 7.00501E-06 7.46464E-06
Ethylbenzene 0.000240771 0.000245822
m-Xylene 0.000146916 0.000151646
o-Xylene 0.000398201 0.000412877
Nonane 2.77443E-06 2.95895E-06
C10+ 8.66550E-07 9.28276E-07
Mass Flow lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h lb/h
Water 0 201324
H2S 0 0
Nitrogen 0 0.322472
Carbon Dioxide 0 4.05157
Methane 0 55.1743
Ethane 0 19.9394
Propane 0 7.93828
Isobutane 0 0.428308
n-Butane 0 1.60553
Isopentane 0 0.348593
n-Pentane 0 0.272076
2-Methylpentane 0 0.0539150
3-Methylpentane 0 0.0712103
n-Hexane 0 0.0356015
Methylcyclopentane 0 0.0766721
Benzene 0 0.521571
2-Methylhexane 0 0.0166897
3-Methylhexane 0 0.0136120
Heptane 0 0.0263654
Methylcyclohexane 0 0.0927563
Toluene 0 0.941038
Octane 0 0.0150351
Ethylbenzene 0 0.495128
m-Xylene 0 0.305442
o-Xylene 0 0.831605
Nonane 0 0.00595983
C10+ 0 0.00186971
Process Streams Well Stream HP Separator Gas HP Separator Water HP Separator Oil OT Flash Gas Sales Oil Gas Water Oil Produced Water PWT Flash Gas Oil W/B Water W/B 1 3 LP Separator Oil
Phase: Heavy Liquid Status Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved Solved
Property Units
Temperature °F 70.0 74.4472
Pressure psig 232 232
Mole Fraction Vapor % 0 0
Mole Fraction Light Liquid % 0 0
Mole Fraction Heavy Liquid % 100 100
Molecular Weight lb/lbmol 18.0 18.0165
Mass Density lb/ft^3 62.3 62.2165
Molar Flow lbmol/h 0.0 11179.6
Mass Flow lb/h 0.0 201417
Vapor Volumetric Flow MCFH 0.0 3.23736
Liquid Volumetric Flow Mbbl/d 0.0 13.8384
Std Vapor Volumetric Flow MMSCFD 0.0 101.820
Std Liquid Volumetric Flow Mbbl/d 0.0 13.8171
Compressibility 0.013 0.0124631
Specific Gravity 0.998 0.997555
API Gravity 10.1 10.0503
Enthalpy MMBtu/h 0.0 -1373.90
Mass Enthalpy Btu/lb -6825.5 -6821.16
Mass Cp Btu/(lb*°F) 1.0 0.982701
Ideal Gas CpCv Ratio 1.326 1.32559
Dynamic Viscosity cP 1.0 0.941676
Kinematic Viscosity cSt 1.0 0.944876
Thermal Conductivity Btu/(h*ft*°F) 0.3 0.348511
Surface Tension lbf/ft 0.005 0.00500564
Net I.G. Heating Value Btu/ft^3 0.5 0.440061
Net Liquid Heating Value Btu/lb -1049.8 -1050.03
Gross I.G. Heating Value Btu/ft^3 50.8 50.7749
Gross Liquid Heating Value Btu/lb 10.5 10.2
Page 1 of 3
October 7, 2013
FESCO, Ltd.
1100 FESCO Avenue - Alice, Texas 78332
For: Antero Resources Appalachian Corp.
1625 17th Street
Denver, Colorado 80202
Sample: Sweeny No. 2H (Forest Well Pad)
Separator Hydrocarbon Liquid
Sampled @ 265 psig & 72 °F
Date Sampled: 09/20/13 Job Number: 35822.002
CHROMATOGRAPH EXTENDED ANALYSIS - GPA 2186-M
COMPONENT
Nitrogen
MOL %
0.016
LIQ VOL %
0.004
WT %
0.005
Carbon Dioxide 0.000 0.000 0.000
Methane 6.555 2.493 1.079
Ethane 6.561 3.938 2.025
Propane 5.950 3.679 2.693
Isobutane 1.825 1.340 1.088
n-Butane 4.352 3.079 2.596
2,2 Dimethylpropane 0.094 0.081 0.070 Isopentane 2.955 2.425 2.188
n-Pentane 3.109 2.529 2.302
2,2 Dimethylbutane 0.233 0.218 0.206
Cyclopentane 0.000 0.000 0.000
2,3 Dimethylbutane 0.371 0.341 0.328
2 Methylpentane 2.077 1.935 1.837
3 Methylpentane 1.448 1.327 1.281
n-Hexane 3.097 2.858 2.739 Heptanes Plus 61.357 73.752 79.565
Totals: 100.000 100.000 100.000
Characteristics of Heptanes Plus:
Specific Gravity ------------------------------- 0.7476 (Water=1)
°API Gravity ----------------------------------- 57.76 @ 60°F
Molecular Weight ---------------------------- 126.4 Vapor Volume --------------------------------- 18.78 CF/Gal Weight ------------------------------------------ 6.23 Lbs/Gal
Characteristics of Total Sample:
Specific Gravity ------------------------------- 0.6930 (Water=1)
°API Gravity ----------------------------------- 72.68 @ 60°F Molecular Weight----------------------------- 97.4 Vapor Volume --------------------------------- 22.57 CF/Gal
Weight ------------------------------------------ 5.77 Lbs/Gal
Base Conditions: 14.850 PSI & 60 °F Certified: FESCO, Ltd. - Alice, Texas
Analyst: XG
Processor: JCdjv David Dannhaus 361-661-7015
Cylinder ID: W-1002
Page 2 of 3
FESCO, Ltd. Job Number: 35822.002
TANKS DATA INPUT REPORT
COMPONENT
Carbon Dioxide
Mol %
0.000
LiqVol %
0.000
Wt %
0.000
Nitrogen 0.016 0.004 0.005
Methane 6.555 2.493 1.079
Ethane 6.561 3.938 2.025 Propane 5.950 3.679 2.693
Isobutane 1.825 1.340 1.088
n-Butane 4.446 3.160 2.665
Isopentane 2.955 2.425 2.188
n-Pentane 3.109 2.529 2.302
Other C-6's 4.129 3.821 3.652
Heptanes 10.940 10.981 11.026 Octanes 16.323 17.415 18.233
Nonanes 9.129 11.236 11.888
Decanes Plus 20.852 30.674 34.062
Benzene 0.102 0.064 0.082
Toluene 0.662 0.498 0.626
E-Benzene 1.009 0.874 1.099
Xylenes 2.340 2.009 2.549
n-Hexane 3.097 2.858 2.739
2,2,4 Trimethylpentane 0.000 0.000 0.000
Totals: 100.000 100.000 100.000
Characteristics of Total Sample:
Specific Gravity --------------------------------------- 0.6930 (Water=1)
°API Gravity ------------------------------------------- 72.68 @ 60°F
Molecular Weight------------------------------------- 97.4 Vapor Volume ---------------------------------------- 22.57 CF/Gal
Weight -------------------------------------------------- 5.77 Lbs/Gal
Characteristics of Decanes (C10) Plus:
Specific Gravity --------------------------------------- 0.7696 (Water=1)
Molecular Weight------------------------------------- 159.2
Characteristics of Atmospheric Sample:
°API Gravity ------------------------------------------- 61.33 @ 60°F
Reid Vapor Pressure (ASTM D-5191)---------- 2.65 psi
QUALITY CONTROL CHECK
Sampling Conditions
Test Samples
Cylinder Number ------ W-1002* T-3030
Pressure, PSIG 265 232 231 Temperature, °F 72 70 70
* Sample used for analysis
FESCO, Ltd. Job Number: 35822.002
TOTAL EXTENDED REPORT
COMPONENT
Nitrogen
Mol %
0.016
LiqVol %
0.004
Wt %
0.005
Carbon Dioxide 0.000 0.000 0.000
Methane 6.555 2.493 1.079
Ethane 6.561 3.938 2.025
Propane 5.950 3.679 2.693 Isobutane 1.825 1.340 1.088
n-Butane 4.352 3.079 2.596
2,2 Dimethylpropane 0.094 0.081 0.070
Isopentane 2.955 2.425 2.188
n-Pentane 3.109 2.529 2.302
2,2 Dimethylbutane 0.233 0.218 0.206
Cyclopentane 0.000 0.000 0.000 2,3 Dimethylbutane 0.371 0.341 0.328
2 Methylpentane 2.077 1.935 1.837
3 Methylpentane 1.448 1.327 1.281
n-Hexane 3.097 2.858 2.739
Methylcyclopentane 0.667 0.530 0.576
Benzene 0.102 0.064 0.082
Cyclohexane 0.624 0.476 0.539
2-Methylhexane 2.715 2.833 2.792
3-Methylhexane 2.221 2.288 2.283
2,2,4 Trimethylpentane 0.000 0.000 0.000
Other C-7's 1.061 1.073 1.080
n-Heptane 3.652 3.781 3.755 Methylcyclohexane 3.129 2.823 3.153
Toluene 0.662 0.498 0.626
Other C-8's 9.393 10.222 10.624
n-Octane 3.801 4.370 4.455
E-Benzene 1.009 0.874 1.099
M & P Xylenes 0.720 0.627 0.784
O-Xylene 1.620 1.383 1.765
Other C-9's 6.182 7.514 8.009 n-Nonane 2.948 3.722 3.879
Other C-10's 6.082 8.124 8.817
n-decane 2.003 2.760 2.925
Undecanes(11) 5.075 6.955 7.656 Dodecanes(12) 2.899 4.291 4.789
Tridecanes(13) 1.869 2.966 3.356
Tetradecanes(14) 1.118 1.901 2.180
Pentadecanes(15) 0.652 1.188 1.379
Hexadecanes(16) 0.379 0.738 0.864 Heptadecanes(17) 0.250 0.514 0.607
Octadecanes(18) 0.184 0.399 0.475
Nonadecanes(19) 0.121 0.274 0.328 Eicosanes(20) 0.077 0.181 0.218
Heneicosanes(21) 0.047 0.115 0.140
Docosanes(22) 0.032 0.081 0.099 Tricosanes(23) 0.020 0.054 0.066
Tetracosanes(24) 0.015 0.040 0.050
Pentacosanes(25) 0.009 0.027 0.033
Hexacosanes(26) 0.006 0.017 0.021
Heptacosanes(27) 0.004 0.012 0.016
Octacosanes(28) 0.003 0.009 0.011
Nonacosanes(29) 0.002 0.008 0.010
Triacontanes(30) 0.002 0.005 0.007
Hentriacontanes Plus(31+) 0.003 0.012 0.016
Total 100.000 100.000 100.000
Page 3 of 3
FESCO, Ltd.
1100 Fesco Avenue - Alice, Texas 78332
October 15, 2013
For: Antero Resources Appalachian Corp. Date Sampled: 09/20/13
1625 17th Street
Denver, Colorado 80202 Date Analyzed: 10/02/13
Sample: Sweeny No. 2H (Forest Well Pad) Job Number: J35822
FLASH LIBERATION OF HYDROCARBON LIQUID
Separator HC Liquid Stock Tank
Pressure, psig 265 0
Temperature, °F 72 70
Gas Oil Ratio (1) ------ 209
Gas Specific Gravity (2) ------ 1.225
Separator Volume Factor (3) 1.1348 1.000
STOCK TANK FLUID PROPERTIES
Shrinkage Recovery Factor (4) 0.8812
Oil API Gravity at 60 °F 61.33
Reid Vapor Pressure, psi (5) 2.65
Quality Control Check
Sampling Conditions Test Samples
Cylinder No. ------ W-1002* T-3030
Pressure, psig 265 232 231
Temperature, °F 72 70 70
(1) - Scf of flashed vapor per barrel of stock tank oil
(2) - Air = 1.000
(3) - Separator volume / Stock tank volume
(4) - Fraction of first stage separator liquid
(5) - Absolute pressure at 100 deg F
Analyst: M. G.
* Sample used for flash study
Base Conditions: 14.85 PSI & 60 °F
Certified: FESCO, Ltd. - Alice, Texas
David Dannhaus 361-661-7015
Page 1 of 2
October 3,2013
FESCO, Ltd.
1100 Fesco Ave. - Alice, Texas 78332
For: Antero Resources Appalachian Corp.
1625 17th Street
Denver, Colorado 80202
Sample: Sweeny No. 2H (Forest Well Pad)
Gas Evolved from Hydrocarbon Liquid Flashed
From 265 psig & 72 °F to 0 psig & 70 °F
Date Sampled: 09/20/13 Job Number: 35822.001
CHROMATOGRAPH EXTENDED ANALYSIS - SUMMATION REPORT
COMPONENT MOL% GPM
Hydrogen Sulfide* < 0.001
Nitrogen 0.042
Carbon Dioxide 0.128
Methane 33.021
Ethane 28.999 7.817
Propane 19.505 5.416
Isobutane 3.942 1.300
n-Butane 7.039 2.237
2-2 Dimethylpropane 0.112 0.043
Isopentane 2.264 0.835
n-Pentane 1.810 0.661
Hexanes 1.577 0.655
Heptanes Plus 1.561 0.703
Totals 100.000 19.666
Computed Real Characteristics Of Heptanes Plus:
Specific Gravity -------------------------- 3.626 (Air=1)
Molecular Weight ------------------------ 103.80
Gross Heating Value -------------------- 5537 BTU/CF
Computed Real Characteristics Of Total Sample:
Specific Gravity -------------------------- 1.225 (Air=1)
Compressibility (Z) ---------------------- 0.9884
Molecular Weight ------------------------ 35.07
Gross Heating Value
Dry Basis -------------------------------- 2069 BTU/CF
Saturated Basis ------------------------ 2033 BTU/CF
*Hydrogen Sulfide tested in laboratory by: Stained Tube Method (GPA 2377)
Results: 0.063 Gr/100 CF, 1.0 PPMV or 0.0001 Mol %
Base Conditions: 14.850 PSI & 60 Deg F
Analyst: MR
Processor: ANB
Certified: FESCO, Ltd. - Alice, Texas
Cylinder ID: FL# 4 S David Dannhaus 361-661-7015
Page 2 of 2
FESCO, Ltd. Job Number: 35822.001
CHROMATOGRAPH EXTENDED ANALYSIS
TOTAL REPORT
COMPONENT MOL % GPM WT %
Hydrogen Sulfide* < 0.001 < 0.001
Nitrogen 0.042 0.034
Carbon Dioxide 0.128 0.161
Methane 33.021 15.106
Ethane 28.999 7.817 24.867
Propane 19.505 5.416 24.528
Isobutane 3.942 1.300 6.534
n-Butane 7.039 2.237 11.667
2,2 Dimethylpropane 0.112 0.043 0.230
Isopentane 2.264 0.835 4.658
n-Pentane 1.810 0.661 3.724
2,2 Dimethylbutane 0.086 0.036 0.211
Cyclopentane 0.015 0.006 0.030
2,3 Dimethylbutane 0.102 0.042 0.251
2 Methylpentane 0.510 0.213 1.253
3 Methylpentane 0.317 0.130 0.779
n-Hexane 0.547 0.227 1.344
Methylcyclopentane 0.054 0.019 0.130
Benzene 0.020 0.006 0.045
Cyclohexane 0.072 0.025 0.173
2-Methylhexane 0.160 0.075 0.457
3-Methylhexane 0.158 0.073 0.452
2,2,4 Trimethylpentane 0.000 0.000 0.000
Other C7's 0.171 0.075 0.484
n-Heptane 0.197 0.092 0.563
Methylcyclohexane 0.165 0.067 0.462
Toluene 0.038 0.013 0.100
Other C8's 0.264 0.124 0.830
n-Octane 0.066 0.034 0.215
Ethylbenzene 0.003 0.001 0.009
M & P Xylenes 0.019 0.007 0.058
O-Xylene 0.003 0.001 0.009
Other C9's 0.106 0.054 0.382
n-Nonane 0.022 0.012 0.080
Other C10's 0.035 0.021 0.141
n-Decane 0.004 0.002 0.016
Undecanes (11) 0.004 0.002 0.017
Totals 100.000 19.666 100.000
Computed Real Characteristics Of Total Sample:
Specific Gravity --------------------------------- 1.225 (Air=1)
Compressibility (Z) ----------------------------- 0.9884
Molecular Weight ------------------------------- 35.07
Gross Heating Value
Dry Basis ------------------------------------- 2069 BTU/CF
Saturated Basis ----------------------------- 2033 BTU/CF
Tag Name Value Units Timestamp
Accumulated Gas Flow 733909.8 MCF 12/6/2013 11:05:27
Casing Pressure 504.96 PSIA 12/6/2013 11:05:40
Current Day Gas Flow 488.7 MCF 12/6/2013 11:05:27
Differential Pressure 7.88 inH2O 12/6/2013 11:05:27
Flow Rate 3760.18 MCF Per Day 12/6/2013 11:05:27
Pressure 209.88 PSIA 12/6/2013 11:05:27
Previous Day Energy 3854.11 MBTU 12/6/2013 11:05:28
Previous Day Gas Flow 3090.55 MCF 12/6/2013 11:05:28
Temperature 68.16 F 12/6/2013 11:05:27
Tubing Pressure 504.05 PSIA 12/6/2013 11:05:40
Daily AP 3.63 PSIA 12/6/2013 09:00:00
Daily DP 310 inH2O 12/6/2013 09:00:00
Daily Energy 3854.1 MBTU 12/6/2013 09:00:00
Daily Flow 3090.55 MCF 12/6/2013 09:00:00
Daily Tf 70.89 F 12/6/2013 09:00:00
Hourly AP 280.83 PSIA 12/6/2013 09:00:00
Hourly DP 4.8 Inches 12/6/2013 09:00:00
Hourly Energy 175.9 MBTU 12/6/2013 09:00:00
Hourly Flow Time 3600 Seconds 12/6/2013 09:00:00
Hourly Tf 69.9 F 12/6/2013 09:00:00
Hourly Volume 141.1 MCF 12/6/2013 09:00:00
Audited Accumulated Gas Volume MCF
Audited Casing Pressure 526 PSI 12/4/2013 09:00:00
Audited Gas Volume 3849.42 MCF 12/4/2013 09:00:00
Audited Oil Volume 183.7 Barrels 12/4/2013 09:00:00
Audited Tubing Pressure 465 PSI 12/4/2013 09:00:00
Audited Water Volume 0 Barrels 12/4/2013 09:00:00
Argon 0 % 12/6/2013 11:05:33
BTU 1247.06 BTU 12/6/2013 11:05:27
C02 0.1467 % 12/6/2013 11:05:33
Carbon Monoxide 0 % 12/6/2013 11:05:33
Decane 0 % 12/6/2013 11:05:33
Ethane 14.1987 % 12/6/2013 11:05:33
Helium 0 % 12/6/2013 11:05:33
Heptane 0 % 12/6/2013 11:05:33
Hexane 0.5451 % 12/6/2013 11:05:33
Hydrogen 0 % 12/6/2013 11:05:33
Hydrogen Sulfide 0 % 12/6/2013 11:05:33
Iso-Butane 0.5666 % 12/6/2013 11:05:33
Iso-Pentane 0.3749 % 12/6/2013 11:05:33
Methane 77.6927 % 12/6/2013 11:05:33
N2 0.4946 % 12/6/2013 11:05:33
N-Butane 1.1838 % 12/6/2013 11:05:33
Nonane 0 % 12/6/2013 11:05:33
N-Pentane 0.2914 % 12/6/2013 11:05:33
Octane 0 % 12/6/2013 11:05:33
Oxygen 0.0117 % 12/6/2013 11:05:33
Plate Size 3.75 Inches 12/6/2013 11:05:38
Propane 4.4938 % 12/6/2013 11:05:33
SPG 0.7248 12/6/2013 11:05:27
Water 0 % 12/6/2013 11:05:33
Water 0 % 12/6/2013 11:06:26
Antero Resources
Sweeney Unit 2H - Forest Pad
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment J
Class I Legal Advertisement
39.422626 degrees N and -80.873179 degrees W
Pollutants
VOC
NOX
CO2e
CO
SO2
PM2.5
PM10
Lead
Total HAPs
Benzene
Formaldehyde
Xylenes
Attachment J
Air Quality Permit Notice
Edna Monroe Well Pad
Notice of Application
31.0906
0.0323
0.5426
Antero Resources Corporation
Notice is given that Antero Resources Corporation has applied to the West Virginia Department of Environmental
Protection, Division of Air Quality, for a General Permit Registration for an Oil and Natural Gas facility located near
0.84 mile east from the intersection of Purgatory Run Rd. (WV 30/1) and (Conaway Run Rd) WV 48 in Tyler County,
West Virginia.
The applicant estimates the potential to discharge the following Regulated Air Pollutants will be:
TOTALS (tpy):
47.4640
8.9639
18624.3000
Tyler County, West Virginia
The latitude and longitude coordinates are:
Any questions regarding this permit application should be directed to the DAQ at (304) 926-0499, extension 1227,
during normal business hours.
Dated this the __ day of ___________, 2015
By: Antero Resources Corporation
Barry Schatz
Senior Environmental & Regulatory Manager
1615 Wynkoop Street
Denver, CO 80202
2.4698
3.79E-05
2.2301
0.0305
0.0255
0.3655
Startup in operation is planned to begin in January 2016. Written comments will be received by the West Virginia
Department of Environmental Protection, Division of Air Quality, 601 57th Street, SE, Charleston, WV 25304, for at
least 30 calendar days from the date of publication of this notice.
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment K
Electronic Submittal
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015 K-1
Attachment K
Electronic Submittal
Edna Monroe Well Pad
Antero Resources Corporation
Tyler, West Virginia
No electronic submission was made.
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment L
General Permit Registration Application Fee
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment M
Siting Criteria Waiver
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015 M-1
Attachment M
Siting Waiver
Edna Monroe Well Pad
Antero Resources Corporation
Tyler County, West Virginia
A Siting Waiver form is not required because there are no occupied dwelling structures within 300 feet
of Edna Monroe Well Pad.
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment N
Material Safety Data Sheet
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015 N-1
Attachment N
Description of Material Safety Data Sheets (MSDS)
Edna Monroe Well Pad
Antero Resources Corporation
Tyler County, West Virginia
Three generic Material Safety Data Sheets (MSDS), and analysis of the condensate and produced water
of a similar well with the same formation are provided. Antero Resources Corporation has developed its
own MSDS for these materials.
1. Natural Gas: The MSDS for natural gas reflects pipeline quality odorized gas. This is essentially
the same as the material delivered to the metering and downstream gathering lines from the
Antero well pad.
2. Condensate: Condensate is the hydrocarbon liquid that has been separated from raw natural
gas through the well pad gas production unit. The liquid is often characterized as having a
gasoline-like odor and consistency.
3. Produced Water: Produced water is primarily groundwater with residual trace hydrocarbons
that has been withdrawn from the ground during the gas extraction process and then separated
from the natural gas and condensate in the gas production units.
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS SYNONYMS: CNG, Natural Gas, Methane.
* * * Section 1 – PRODUCT AND COMPANY IDENTIFICATION * * * PRODUCT NAME: Dry Field Natural Gas EMERGENCY PHONE: (800) 878-1373 PRODUCT CODES: CAS Reg. No. 68410-63-9 AFTER HOURS: (800) 878-1373 PRODUCER: Antero Resources ADDRESS: 1615 Wynkoop Street CHEMTREC PHONE: (800) 424-9300 Denver, Colorado 80202
* * * Section 2 – HAZARDS IDENTIFICATION * * * GHS Classification: Flammable Gas – Category 1. Gases Under Pressure – Gas. Specific Target Organ Systemic Toxicity (STOT) – Single Exposure Category 2. GHS LABEL ELEMENTS Symbol(s)
Signal Word Danger Hazard Statements Extremely flammable gas. Contains gas under pressure, may explode if heated. May cause damage to central nervous and respiratory systems. Precautionary Statements Prevention Keep away from heat/sparks/open flames/hot surfaces. No smoking. Do not breathe fume/gas/mist/vapors/spray. Wash thoroughly after handling. Do not eat, drink or smoke when using this product.
Page 1 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS Response Leaking gas fire: Do not extinguish, unless leak can be stopped safely. Eliminate all ignition sources if safe to do so. If exposed to gas, or concerned about possible exposure: Call a POISON CENTER or doctor/physician. Storage Protect from sunlight. Store in a well-ventilated place. Store in a secure area. Disposal Dispose of contents/containers in accordance with local/regional/national/international regulations.
* * * Section 3 – COMPOSITION / INFORMATION ON INGREDIENTS * * *
CAS # Component Percent 74-82-8 Methane 95.01 78-84-0 Ethane 3.99 74-98-6 Propane 0.32 106-97-8 Butanes 0.07 109-66-0 Pentanes 0.02 110-54-3 Hexanes 0.01 7727-37-9 Nitrogen 0.35 124-38-9 Carbon Dioxide 0.19 7782-44-7 Oxygen 0.03
Because natural gas is a natural product, composition can vary greatly.
* * * Section 4 – FIRST AID MEASURES * * * First Aid: Eyes In case of freeze burn, cover eyes to protect from light. Flush eyes with running water
for at least fifteen (15) minutes. Following flushing, seek medical attention. First Aid: Skin Remove contaminated clothing. In case of blistering, frostbite or freeze burns, seek
immediate medical attention.
Page 2 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS First Aid: Ingestion Risk of ingestion is extremely low. However, if oral exposure occurs, seek immediate
medical assistance. First Aid: Inhalation Remove person to fresh air. If person is not breathing, provide artificial respiration. If
necessary, provide additional oxygen once breathing is restored if trained to do so. Seek medical attention immediately.
* * * Section 5 – FIRE FIGHTING MEASURES * * *
NFPA 704 Hazard Class Health: 1 Flammability: 4 Instability: 0 (0-Minimal, 1-Slight, 2-Moderate, 3-Serious, 4-Severe) General Fire Hazards See Section 9 for Flammability Properties. Forms a flammable mixture with air. If released, the resulting vapors will disperse with
the prevailing wind. If a source of ignition is present where the vapor exists at a 5 – 15% concentration in air, the vapor will burn along the flame front toward the source of the fuel.
Hazardous Combustion Products Carbon monoxide, carbon dioxide and non-combusted hydrocarbons (smoke). Extinguishing Media Any extinguisher suitable for Class B fires, dry chemical, fire fighting foam, CO2, and
other gaseous agents. However, fire should not be extinguished unless flow of gas can be immediately stopped.
Unsuitable Extinguishing Media None. Fire Fighting Equipment / Instructions Gas fires should not be extinguished unless flow of gas can be immediately stopped.
Shut off gas source and allow gas to burn out. If spill or leak has not ignited, determine
1
4
0
Page 3 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS if water spray may assist in dispersing gas or vapor to protect personnel attempting to
stop leak. Use water to cool equipment, surfaces and piping exposed to fire and excessive heat. For large fire, the use of unmanned hose holders or monitor nozzles may be advantageous to further minimize personnel exposure. Isolate area, particularly around piping. Let the fire burn unless leak can be stopped. Concentrate fire-fighting efforts on objects / materials ignited by the initial fire. Withdraw immediately in the event of a rising sound from a venting safety device.
Firefighting activities that may result in potential exposure to high heat, smoke or toxic
by-products of combustion should require NIOSH-approved pressure-demand self-contained breathing apparatus with full facepiece and full protective clothing.
* * * Section 6 – ACCIDENTAL RELEASE MEASURES * * * Recovery and Neutralization Stop the source of the release, if safe to do so. Materials and Methods for Clean-Up Consider the use of water spray to disperse gas vapors. Do not use water spray to
direct gas vapors toward sewer or drainage systems. Isolate the area until gas has dispersed. Ventilate and gas test area before entering.
Emergency Measures Evacuate nonessential personnel and secure all ignition sources. No road flares,
smoking or flames in hazard area. Consider wind direction. Stay upwind and uphill, if possible. Vapor cloud may be white, but color will dissipate as cloud disperses. Fire and explosion hazard is still present.
Personal Precautions and Protective Equipment Cooling effect of expanding gas from leak may present frostbite / freeze burn hazard.
Wear flame retardant (FR) clothing around un-ignited leak. Wear fire protective clothing around an active fire.
Environmental Precautions Do not flush gas vapors toward sewer or drainage systems. Prevention of Secondary Hazards None. Page 4 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS
* * * Section 7 – HANDLING AND STORAGE * * * Handling Procedures Keep away from flame, sparks and excessive temperatures. Bond and ground
containers. Use only in well ventilated areas. Storage Procedures Natural gas will be contained in the pipeline. Keep away from flame, sparks, excessive
temperatures and open flames. Empty pipeline segments may contain explosive residues from natural gas liquids. Do not cut, heat, weld or expose containers to sources of ignition sections of pipeline unless the sections have been purged of natural gas residues.
Incompatibilities Keep away from strong oxidizers, ignition sources and heat.
* * * Section 8 – EXPOSURE CONTROLS / PERSONAL PROTECTION * * * Component Exposure Limits Methane (74-82-8) ACGIH: 1000 ppm TWA (listed under Aliphatic hydrocarbon gases : Alkane C1-4) Ethane (74-84-0) ACGIH: 1000 ppm TWA (listed under Aliphatic hydrocarbon gases : Alkane C1-4) Propane (74-98-6) ACGIH: 2500 ppm TWA (listed under Aliphatic hydrocarbon gases : Alkane C1-4) Butane (106-97-8) ACGIH: 800 ppm TWA (listed under Aliphatic hydrocarbon gases : Alkane C1-4) Pentanes (109-66-0) ACGIH: 600 ppm TWA (listed under Pentane, all isomers) Hexanes (110-54-3) ACGIH: 50 ppm TWA (listed under n-Hexane)
Page 5 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS Nitrogen (7727-37-9) Simple Asphyxiant Carbon Dioxide (124-38-9) ACGIH: 5000 ppm TWA (listed under Carbon Dioxide) Oxygen (7782-44-7) N/A – Necessary for life Engineering Measures Use adequate ventilation to keep gas and vapor concentrations of this product below
occupational exposure and flammability limits, particularly in confined spaces. Use explosion-proof equipment and lighting in classified / controlled areas.
Personal Protective Equipment: Respiratory Use a NIOSH approved positive-pressure, supplied air respirator with escape bottle or
self-contained breathing apparatus (SCBA) for gas concentrations above occupational exposure limits, for potential for uncontrolled release, if exposure levels are not known, or in an oxygen-deficient atmosphere. CAUTION: Flammability limits (i.e., explosion hazard should be considered when assessing the need to expose personnel to concentrations requiring respiratory protection.
Personal Protective Equipment: Hands Use cold-impervious, insulating flame-retardant (FR) gloves where contact with
pressurized gas may occur. Personal Protective Equipment: Eyes Where there is a possibility of pressurized gas contact, wear splash-proof safety
goggles and faceshield. Personal Protective Equipment: Skin and Body Where contact with pressurized gas may occur, wear flame-retardant (FR) and a
faceshield.
* * * Section 9 – PHYSICAL AND CHEMICAL PROPERTIES * * *
Appearance: Colorless Odor: Odorless to slight
petroleum odor Physical State: Gas pH: ND
Vapor Pressure: 40 atm @ -187°F (-86°C) Vapor Density: 0.6 Boiling Point: -259°F (-162°C) Melting Point: ND
Solubility (H2O): 3.5% Specific Gravity: 0.4 @ -263°F (-164°C)
Page 6 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS
Evaporation Rate: ND VOC: ND Octanol / H2O Coeff.: ND Flash Point: Flammable Gas Flash Point Method: N/A
Lower Flammability Limit: 3.8 – 6.5 Upper Flammability Limit: 13-17 (LFL): (UFL):
Auto Ignition: 900-1170°F (482-632°C) Burning Rate: ND
* * * Section 10 – CHEMICAL STABILITY & REACTIVITY INFORMATION * * * Chemical Stability This is a stable material. Hazardous Reaction Potential Will not occur. Conditions to Avoid Keep away from strong oxidizers, ignition sources and heat. Hazardous Decomposition Products Carbon monoxide, carbon dioxide and non-combusted hydrocarbons (smoke).
* * * Section 11 – TOXICOLOGICAL INFORMATION * * * Acute Toxicity A: General Product Information Methane and ethane, the main components of natural gas, are considered practically
inert in terms of physiological effects. At high concentrations these materials act as simple asphyxiants and may cause death due to lack of oxygen.
B. Component Analysis – LD50/LC50 Methane (74-82-8) Inhalation LC50 Mouse 326 g/m3 2h Ethane (74-84-0) Inhalation LC50 Rat 658 mg/l 4h Propane (74-98-6) Inhalation LC50 Rat 658 mg/l 4h
Page 7 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS Butanes (106-97-8) Inhalation LC50 Rat 658 g/m3 4h Pentanes (109-66-0) Inhalation LD50 Rat 364 g/m3 4h Hexanes (110-54-3) Inhalation LC50 Rat > 20 mg/l 4h Nitrogen (7727-37-9) Simple Asphyxiant Carbon Dioxide (124-38-9) Inhalation LC50 Human 100,000 ppm 1minute Oxygen (7782-44-7) N/A – Necessary for life Potential Health Effects: Skin Corrosion Property / Stimulativeness This product is not reported to have any skin sensitization effects. Generative Cell Mutagenicity This product is not reported to have any mutagenic effects. Carcinogenicity A: General Product Information This product is not reported to have any carcinogenic effects. B: Component Carcinogenicity None of this product's components are listed by ACGIH, IARC, OSHA, NIOSH, or NTP. Reproductive Toxicity This product is not reported to have any reproductive toxicity effects. Specified Target Organ General Toxicity: Single Exposure This product may cause damage to the heart. Specified Target Organ General Toxicity: Repeated Exposure This product is not reported to have any specific target organ repeat effects. Aspiration Respiratory Organs Hazard This product is not reported to have any aspiration hazard effects. Page 8 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS
* * * Section 12 – ECOLOGICAL INFORMATION * * * Ecotoxicity A: General Product Information Keep gas and vapors out of sewers, drainage areas, and waterways. Report spills and
releases, as applicable under Federal and State regulations. B: Component Analysis – Ecotoxicity – Aquatic Toxicity No ecotoxicity data are available for this product's components. Persistance / Degradability No information available. Bioaccumulation No information available. Mobility in Soil No information available.
* * * Section 13 – DISPOSAL CONSIDERATIONS * * * Waste Disposal Instructions See Section 7 for Handling Procedures. See Section 8 for Personal Protective
Equipment Recommendations. Disposal of Contaminated Containers or Packaging Dispose of contents / container in accordance with local / regional / national /
international regulations.
* * * Section 14 – TRANSPORTATION INFORMATION * * * DOT Information Shipping Name: Natural Gas, Compressed UN #: 1971 Hazard Class: 2.1 Placard:
Page 9 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS
* * * Section 15 – REGULATORY INFORMATION * * * Regulatory Information Component Analysis None of this products components are listed under SARA Section 302 (40 CFR 355
Appendix A. n-hexane is listed under SARA Section 313 (40 CFR 372.65). However the
concentration of this component is approximately 0.01 % in compressed natural gas and is therefore far under the reporting threshold for the chemical.
n-hexane is listed under CERCLA (40 CFR 302.4). However the concentration of this
component is approximately 0.01 % in compressed natural gas and is therefore far under the reporting threshold for the chemical.
SARA Section 311/312 – Hazard Classes Acute Health Chronic Health Fire Sudden Release of Pressure Reactive --- --- X X --- SARA Section 313 – Supplier Notification This product contains one chemical (n-Hexane) that is subject to the reporting
requirements of section 313 of the Emergency Planning and Community Right-to-know act (EPCRA) of 1986 and of 40 CFR 372. However the concentration of this component is approximately 0.01 % in compressed natural gas and is therefore far under the reporting threshold for the chemical.
State Regulations Component Analysis – State The following components appear on one or more of the following state hazardous
substances lists:
Component CAS CA MA MN NJ PA RI Methane 74-82-8 No No Yes Yes Yes No
Ethane 78-84-0 No No Yes Yes Yes No
Propane 74-98-6 No No Yes Yes Yes Yes
Butane 106-97-8 Yes No Yes Yes Yes Yes
Pentanes 109-66-0 Yes No Yes Yes Yes Yes
Hexanes 110-54-3 Yes Yes Yes Yes Yes Yes
Nitrogen 7727-37-9 No No No No No No
Carbon Dioxide 124-38-9 Yes No Yes Yes Yes Yes
Oxygen 7782-44-7 No No No No No No
Page 10 of 11
SAFETY DATA SHEET
Material Name: Dry Field Natural Gas US GHS
* * * Section 16 – OTHER INFORMATION * * *
NFPA® Hazard Rating Health 1 Fire 4 Reactivity 0 HMIS® Hazard Rating Health 1 Moderate Fire 4 Severe Physical 0 Minimal * Chronic Key/Legend EPA = Environmental Protection Agency; TSCA = Toxic Substance Control Act: ACGIH
= American Conference of Governmental Industrial Hygienists; IARC = International Agency for Research on Cancer; NIOSH = National Institute for Occupational Safety and Health; NTP = National Toxicology Program; OSHA = Occupational Safety and Health Administration; NJTSR = New Jersey Trade Secret Registry.
Literature References None Other Information The information presented herein has been compiled from sources considered to be
dependable, and is accurate and reliable to the best of our knowledge and belief, but is not guaranteed to be so. Since conditions of use are beyond our control, we make no warranties, expressed or implied, except those that may be contained in our written contract of sale or acknowledgment.
Vendor assumes no responsibility for injury to vendee or third persons proximately
caused by the material if reasonable safety procedures are not adhered to as stipulated in the data sheet. Additionally, vendor assumes no responsibility for injury to vendee or third persons proximately caused by abnormal use of the material, even if reasonable safety procedures are followed. Furthermore, vendee assumes the risk in their use of the material.
Date of Preparation: January 30, 2014 Date of Last Revision: March 4, 2014
End of Sheet
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SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS SYNONYMS: Drips; Condensate; Field Condensate; Gas Well Condensate; High
Pressure Inlet Liquids; Lease Condensate; Natural Gas Liquids; Pipeline Liquids
* * * Section 1 – PRODUCT AND COMPANY IDENTIFICATION * * * PRODUCT NAME: Natural Gas Condensate EMERGENCY PHONE: (800) 878-1373 PRODUCT CODES: 64741-47-5 AFTER HOURS: (800) 878-1373 PRODUCER: Antero Resources ADDRESS: 1615 Wynkoop Street CHEMTREC PHONE: (800) 424-9300 Denver, Colorado 80202
* * * Section 2 – HAZARDS IDENTIFICATION * * * GHS Classification: Flammable Liquids – Category 2. Acute Toxicity Inhalation – Category 3 Germ Cell Mutagenicity – Category 1B Carcinogenicity – Category 1A Specific Target Organ Systemic Toxicity (STOT) – Single Exposure Category 3 Specific Target Organ Systemic Toxicity (STOT) – Repeat Exposure Category 1 Aspiration Toxicity – Category 1 Toxic to the Aquatic Environment Acute – Category 3 GHS LABEL ELEMENTS Symbol(s)
Signal Word Danger Page 1 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Hazard Statements Highly flammable liquid and vapor. Toxic if inhaled. May cause genetic defects. May cause cancer. May cause respiratory irritation. May cause drowsiness or dizziness. May cause damage to organs (liver, kidneys, blood, nervous system, and skin) through prolonged or repeated exposure. May be fatal if swallowed and enters airways. Harmful to aquatic life. Precautionary Statements Prevention Keep away from heat/sparks/open flames/hot surfaces. No smoking. Keep container tightly closed. Ground/bond container and receiving equipment. Use explosion-proof electrical/ventilating/lighting equipment. Use only non-sparking tools. Take precautionary measures against static discharge. Wear protective gloves/protective clothing/eye protection/face protection. Do not breathe gas/mist/vapors/spray. Do not handle until all safety precautions have been read and understood. Wash thoroughly after handling. Do not eat, drink or smoke when using this product. Use only outdoors or in a well-ventilated area. Avoid release to the environment. Response If on SKIN (or hair): Wash with plenty of soap and water. Remove / Take off all contaminated clothing immediately. Rinse skin with water/shower. If INHALED: Remove victim to fresh air and keep comfortable for breathing. Call a poison center/doctor if the victim feels unwell. If SWALLOWED: Immediately call a poison center or doctor / physician. Do not Induce vomiting. If exposed or concerned: Get medical advice/attention. In case of fire: Use water spray, fog or fire-fighting foam. Storage Store in a well-ventilated place. Keep cool. Store in a secure area.
Page 2 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Disposal Dispose of contents/containers in accordance with local/regional/national/international regulations.
* * * Section 3 – COMPOSITION / INFORMATION ON INGREDIENTS * * *
CAS # Component Percent 111-65-9 Octanes 25 - 95 142-82-5 Heptanes 25 - 95 110-54-3 Hexanes as n-Hexane 25 - 95 109-66-0 Pentanes as n-Pentane 5 - 70 106-97-8 N-butane 0 - 45 74-98-6 Propane 0 - 15 78-84-0 Ethane 0 - 5 71-43-2 Benzene < 1
108-88-3 Toluene < 1
1330-20-7 m-,o-,p-Xylene < 1
Because natural gas condensate is a natural product, composition can vary greatly.
* * * Section 4 – FIRST AID MEASURES * * * First Aid: Eyes Flush eyes with clean running water for at least fifteen (15) minutes. Following flushing,
seek medical attention. First Aid: Skin Remove contaminated clothing. Wash contaminated areas thoroughly with soap and
water or waterless hand cleanser. Obtain medical attention if irritation or redness develops. Wash contaminated clothing before reuse.
First Aid: Ingestion (swallowing) DO NOT INDUCE VOMITING. Do not give liquids. Obtain immediate medical
attention. If spontaneous vomiting occurs, lean the victim forward to reduce the risk of aspiration. Monitor for breathing difficulties. Small amounts of material which enter the mouth should be rinsed out until the taste is dissipated.
Page 3 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS First Aid: Inhalation (breathing) Remove person to fresh air. If person is not breathing, provide artificial respiration. If
necessary, provide additional oxygen once breathing is restored if trained to do so. Seek medical attention immediately.
* * * Section 5 – FIRE FIGHTING MEASURES * * *
NFPA 704 Hazard Class Health: 1 Flammability: 4 Instability: 0 (0-Minimal, 1-Slight, 2-Moderate, 3-Serious, 4-Severe) General Fire Hazards See Section 9 for Flammability Properties. Extremely flammable. Vapors may be ignited rapidly when exposed to heat, spark,
open flame, or other source of ignition (e.g., static electricity, pilot lights, mechanical / electrical equipment, and electronic devices such as cell phones, computers, calculators, and pagers which have not been certified as intrinsically safe). Flammable vapors can burn in the open or explode in confined spaces. Vapors are heavier than air, and may travel distances to an ignition source and flash back. Runoff to sewer systems may cause fire or explosion.
Hazardous Combustion Products Carbon monoxide, carbon dioxide and non-combusted hydrocarbons (smoke). Extinguishing Media SMALL FIRES: Any extinguisher suitable for Class B fires, dry chemical, firefighting
foam, water spray, carbon dioxide (CO2), or other gaseous extinguishing agents. Use caution when applying CO2 in confined spaces.
LARGE FIRES: Water spray, fog or fire-fighting foam. Water may be ineffective for
fighting the fire, but may be used to cool fire-exposed containers. Unsuitable Extinguishing Media None
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SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Fire Fighting Equipment / Instructions Small fires in the beginning stage may typically be extinguished using handheld portable
fire extinguishers and other firefighting equipment. Isolate area around container involved in fire. Cool tanks, shells, and containers exposed to fire and excessive heat with water. For massive fires the use of unmanned hose holders or monitor nozzles may be advantageous to minimize personnel exposure. Major fires may require withdrawal, allowing the tank to burn. Large storage tank fires typically require specially trained personnel and equipment to extinguish the fire, often including the need for properly applied firefighting foam.
Firefighting activities that may result in potential exposure to high heat, smoke or toxic
by-products of combustion should require NIOSH/MSHA- approved pressure-demand self-contained breathing apparatus with full face piece and full protective clothing.
* * * Section 6 – ACCIDENTAL RELEASE MEASURES * * * Recovery and Neutralization Contain and stop the source of the spill, if safe to do so.
Materials and Methods for Clean-Up Notify relevant authorities in accordance with all applicable regulations. Immediate
cleanup of any spill is recommended. Dike far ahead of spill for later recovery or disposal. Absorb spill with inert material such as sand or vermiculite, and place in suitable container for disposal. If spilled on water remove with appropriate methods (e.g. skimming, booms or absorbents). In case of soil contamination, remove contaminated soil for remediation or disposal, in accordance with local regulations.
Recommended measures are based on the most likely spillage scenarios for this
material; however local conditions and regulations may influence or limit the choice of appropriate actions to be taken.
Emergency Measures Evacuate nonessential personnel and secure all ignition sources. No road flares,
smoking or flames in hazard area. Consider wind direction. Stay upwind and uphill, if possible. Vapor cloud may be white, but color will dissipate as cloud disperses. Fire and explosion hazard is still present.
Personal Precautions and Protective Equipment Response and clean-up crews must be properly trained and must utilize proper
protective equipment (see Section 8). Extremely flammable. Spillages of liquid product will create a fire hazard and may form an explosive atmosphere. Keep all sources of
Page 5 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS
ignition and hot metal surfaces away from spill/release if safe to do so. The use of explosion-proof electrical equipment is recommended. Stay upwind and
away from spill/release. Avoid direct contact with material. For large spillages, notify persons downwind of the spill/release, isolate immediate hazard area and keep unauthorized personnel out. Wear appropriate protective equipment, including respiratory protection, as conditions warrant (see Section 8). See Sections 2 and 7 for additional information on hazards and precautionary measures.
Environmental Precautions Protect bodies of water by diking, absorbents, or absorbent boom, if possible. Do not
flush down sewer or drainage systems, unless system is designed and permitted to handle such material. The use of firefighting foam may be useful in certain situations to reduce vapors. If spill occurs on water notify appropriate authorities and advise shipping of any hazard. Spills into or upon navigable waters, the contiguous zone, or adjoining shorelines that cause a sheen or discoloration on the surface of the water, may require notification of the National Response Center (phone number 800-424-8802).
Prevention of Secondary Hazards None
* * * Section 7 – HANDLING AND STORAGE * * * Handling Procedures Keep away from flame, sparks and excessive temperatures. Bond and ground
containers. Use non-sparking tools. Use only outdoors or in well ventilated areas. Wear protective gloves / clothing and eye / face protection. Wash thoroughly after handling. Use good personal hygiene practices and wear appropriate personal protective equipment (see section 8).
Storage Procedures Store only in approved containers. Bond and ground containers. Keep away from
flame, sparks, excessive temperatures and open flames. Keep containers closed and clearly labeled. Empty product containers or vessels may contain explosive vapors. Do not pressurize, cut, heat, weld or expose containers to sources of ignition.
Store in a well-ventilated area. This storage area should comply with NFPA 30
"Flammable and Combustible Liquid Code". Avoid storage near incompatible materials. The cleaning of tanks previously containing this product should follow API Recommended Practice (RP) 2013 "Cleaning Mobile Tanks In Flammable and Combustible Liquid Service" and API RP 2015 "Cleaning Petroleum Storage Tanks."
Page 6 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Incompatibilities Keep away from strong oxidizers, ignition sources and heat.
* * * Section 8 – EXPOSURE CONTROLS / PERSONAL PROTECTION * * * Component Exposure Limits Octanes (111-65-9) ACGIH: 300 ppm TWA (listed under Octane, all isomers) Heptanes (142-82-5) ACGIH: 400 ppm TWA (listed under n-Heptane) n-Hexane (110-54-3) ACGIH: 20 ppm TWA (listed under n-Hexane) n-Pentane (109-66-0) ACGIH: 600 ppm TWA (listed under Pentane, all isomers) n-Butane (106-97-8) ACGIH: 600 ppm TWA (listed under n-Butane) Propane (74-98-6) ACGIH: 1000 ppm TWA (listed under Aliphatic hydrocarbon gases C1-C4) Ethane (74-84-0) ACGIH: 1000 ppm TWA (listed under Aliphatic hydrocarbon gases C1-C4) Benzene (71-43-2) ACGIH: 0.5 ppm (TWA); NIOSH: 0.1 ppm (TWA); OSHA 1 ppm (TWA) Toluene (108-88-3) ACGIH: 20 ppm TWA (listed under Toluene) m-, o-, p-Xylene (1330-20-7) ACGIH: 100 ppm TWA (listed under Xylene o, m & p isomers)
Page 7 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Engineering Measures Use adequate ventilation to keep vapor concentrations of this product below
occupational exposure and flammability limits, particularly in confined spaces. Use explosion-proof equipment and lighting in classified / controlled areas.
Personal Protective Equipment: Respiratory Use a NIOSH-approved positive-pressure, supplied air respirator with escape bottle or
self-contained breathing apparatus (SCBA) for gas concentrations above occupational exposure limits, for potential for uncontrolled release, if exposure levels are not known, or in an oxygen-deficient atmosphere (oxygen content less than 19.5 percent). A respiratory program that meets or is equivalent to OSHA 29 CFR 1910.134 and ANSI Z88.2 should be followed whenever workplace conditions warrant the use of a respirator.
If benzene concentrations equal or exceed applicable exposure limits, OSHA
requirements for personal protective equipment, exposure monitoring, and training may apply (29 CFR 1910.1028 – Benzene).
CAUTION: Flammability limits (i.e., explosion hazard should be considered when
assessing the need to expose personnel to concentrations requiring respiratory protection.
Personal Protective Equipment: Hands Gloves constructed of nitrile or neoprene are recommended. Personal Protective Equipment: Eyes Safety glasses or goggles are recommended where there is a possibility of splashing or
spraying. Eye protection that meets or exceeds ANSI Z.87.1 is recommended. Depending on conditions of use, a face shield may be necessary.
Personal Protective Equipment: Skin and Body Chemical protective clothing such as of E.I. DuPont TyChem®, Saranex® or equivalent
recommended based on degree of exposure. Note: The resistance of specific material may vary from product to product as well as with degree of exposure. Consult manufacturer specifications for further information.
Hygiene Measures Emergency eye wash capability should be available in the near proximity to operations
presenting a potential splash exposure. Use good personal hygiene practices. Avoid repeated and/or prolonged skin exposure. Wash hands before eating, drinking, smoking, or using toilet facilities. Do not use as a cleaning solvent on the skin. Do not use gasoline or solvents (naphtha, kerosene, etc.) for washing this product from
Page 8 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS
exposed skin areas. Waterless hand cleaners are effective. Promptly remove contaminated clothing and launder before reuse. Use care when laundering to prevent the formation of flammable vapors which could ignite via washer or dryer. Consider the need to discard contaminated leather shoes and gloves.
* * * Section 9 – PHYSICAL AND CHEMICAL PROPERTIES * * * Appearance: Colorless to straw yellow Odor: Aromatic, Gasoline; Physical State: Liquid pH: ND Vapor Pressure: 110 – 200 psia (Reid VP)
@ 100°F/37.8°C
Vapor Density (air = 1): > 1
Boiling Point: Approx. 85 - 437°F (39 – 200°C)
Melting Point: ND
Solubility (H2O): Insoluble to slightly soluble
Specific Gravity: AP 0.62-0.76 (varies)
Evaporation Rate: High VOC: ND Octanol / H2O Coeff.: ND Flash Point: -40°F
-40°C Flash Point Method: Tag Closed Cup (TCC) Lower Flammability Limit: ND (NFPA Gasoline 1.4) Upper Flammability Limit: ND (NFPA Gasoline 7.6) (LFL): (UFL): Auto Ignition: AP 480°F (250°C) Burning Rate: ND
* * * Section 10 – CHEMICAL STABILITY & REACTIVITY INFORMATION * * * Chemical Stability This is a stable material.
Hazardous Reaction Potential Will not occur. Conditions to Avoid Keep away from ignition sources and high temperatures. Hazardous Decomposition Products Carbon monoxide, carbon dioxide and non-combusted hydrocarbons (smoke). Page 9 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS
* * * Section 11 – TOXICOLOGICAL INFORMATION * * * Acute Toxicity A: General Product Information Harmful if swallowed. B. Component Analysis – LD50/LC50 Octanes (111-65-9) Inhalation LC50 rat = 118,000 mg/m3 / 4H Heptanes (142-82-5) Inhalation LC50 rat = 103,000 mg/m3 / 4H Hexanes as n-Hexane (110-53-3) Inhalation LC50 rat = 48,000 ppm / 4H Pentanes as n-Pentane (109-66-0) Inhalation LC50 rat = 364,000 mg/m3 / 4H Butanes as n-Butane (106-97-8) Inhalation LC50 rat 658,000 mg/l / 4H Propane (74-98-6) Inhalation LC50 Rat > 800,000 ppm / 0.25H Ethane (74-84-0) Inhalation LC50 Rat 658,000 mg/l / 4H Benzene (71-43-2) Inhalation LC50 Rat 44,700 mg/m3 /
Toluene (108-88-3) Inhalation LD50 Rat 12/5 mg/l / 4H m-, o-, p-Xylene (1330-20-7) Inhalation LC50 Rat 5000 ppm / 4H Potential Health Effects: Skin Corrosion Property / Stimulativeness May cause skin irritation with prolonged or repeated contact. Liquid may be absorbed
through the skin in toxic amounts if large areas of skin are exposed repeatedly.
Page 10 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Potential Health Effects: Eye Critical Damage / Stimulativeness Contact with eyes may cause moderate irritation. Potential Health Effects: Ingestion (swallowing) Ingestion may cause gastrointestinal disturbances, including irritation, nausea, vomiting
and diarrhea, and central nervous system (brain) effects similar to alcohol intoxication. In severe cases, tremors, convulsions, loss of consciousness, coma, respiratory arrest, and death may occur.
Potential Health Effects: Inhalation (breathing) Excessive exposure may cause irritations to the nose, throat, lungs and respiratory
tract. Central nervous system (brain) effects may include headache, dizziness, loss of balance and coordination, unconsciousness, coma, respiratory failure, and death.
Respiratory Organs Sensitization / Skin Sensitization This product is not reported to have any skin sensitization effects. Generative Cell Mutagenicity May cause genetic defects. Some crude oils and crude oil fractions have been positive
in mutagenicity studies. Carcinogenicity A: General Product Information May cause cancer. This product contains benzene, although at very low concentrations. Human health
studies indicate that prolonged and/or repeated overexposure to benzene may cause damage to the blood-forming system (particularly bone marrow), and serious blood disorders such as aplastic anemia and leukemia. Benzene is listed as a human carcinogen by the NTP, IARC, OSHA and ACGIH.
Exposure to light hydrocarbons in the same boiling range as this product have been
associated in animal studies with effects to the central nervous system, peripheral nervous system, liver, and kidneys. The significance of these animal models to predict similar human response is uncertain. Observing good work practices and personal hygiene procedures (Sections 7 and 8) can minimize potential risks to humans.
B: Component Carcinogenicity Benzene (71-43-2) ACGIH: A1 - Confirmed Human Carcinogen OSHA: 5 ppm STEL (Cancer hazard, Flammable, See 29 CFR 1910.1028,
15 min); 0.5 ppm Action Level; 1 ppm TWA NIOSH: potential occupational carcinogen NTP: Known Human Carcinogen (Select Carcinogen) Page 11 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS IARC: Monograph 100F [in preparation]; Supplement 7 [1987]; Monograph
29 [1982] (Group 1 (carcinogenic to humans)) Reproductive Toxicity This product is not reported to have any reproductive toxicity effects. Specified Target Organ General Toxicity: Single Exposure This product is not reported to have any specific target organ general toxicity single
exposure effects. Specified Target Organ General Toxicity: Repeated Exposure May cause damage to organs (liver, kidneys, blood, nervous system and skin) through
prolonged or repeated exposure. Aspiration Respiratory Organs Hazard The major health threat of ingestion occurs from the danger of aspiration (breathing) of
liquid drops into the lungs, particularly from vomiting. Aspiration may result in chemical pneumonia (fluid in the lungs), severe lung damage, respiratory failure and even death.
* * * Section 12 – ECOLOGICAL INFORMATION * * *
Ecotoxicity A: General Product Information Keep out of sewers, drainage areas, and waterways. Report spills and releases, as
applicable under Federal and State regulations. B: Component Analysis – Ecotoxicity – Aquatic Toxicity Benzene (71-43-2) Test and Species Conditions 96 Hr LC50 Pimephales promelas
10.7-14.7 mg/L [flow-through]
96 Hr LC50 Oncorhynchus mykiss 5.3 mg/L [flow-through]
96 Hr LC50 Lepomis macrochirus 22.49 mg/L [static]
96 Hr LC50 Poecilia reticulata 28.6 mg/L [static]
96 Hr LC50 Pimephales promelas 22330-41160 μg/L [static]
96 Hr LC50 Lepomis macrochirus 70000-142000 μg/L [static]
72 Hr EC50 Pseudokirchneriella subcapitata 29 mg/L
48 Hr EC50 Daphnia magna 8.76 - 15.6 mg/L [static]
48 Hr EC50 Daphnia magna 10 mg/L
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SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Natural Gas condensates (68919-39-1) Test and Species Conditions 96 Hr LC50 Alburnus alburnus 119 mg/L [static]
96 Hr LC50 Cyprinodon variegatus 82 mg/L [static] 72 Hr EC50 Pseudokirchneriella subcapitata 56 mg/L
24 Hr EC50 Daphnia magna 170 mg/L
Persistence / Degradability No information available Bioaccumulation No information available Mobility in Soil No information available
* * * Section 13 – DISPOSAL CONSIDERATIONS * * * Waste Disposal Instructions See Section 7 for Handling Procedures. See Section 8 for Personal Protective
Equipment Recommendations. Disposal of Contaminated Containers or Packaging Recover or recycle if possible. It is the responsibility of the generator to determine the
toxicity and physical properties of the material generated so as to properly classify the waste and ensure disposal methods comply with applicable regulations.
This material, if discarded should be fully characterized for ignitability (D001), reactivity (D003) and benzene (D018) prior to disposal (40 CFR261). Use which results in chemical or physical change or contamination may subject it to regulation as a hazardous waste. Along with properly characterizing all waste materials, consult state and local regulations regarding the proper disposal of this material. Do not dispose of by draining onto the ground. This will result in soil and groundwater contamination. Waste arising from spillage or tank cleaning should be disposed of in accordance with applicable regulations.
Container contents should be completely used and containers should be emptied prior
to discard. Container rinsate could be considered a RCRA hazardous waste and must be disposed of with care and in full compliance with federal, state and local regulations. Larger empty containers, such as drums, should be returned to the distributor or to a qualified drum reconditioner. To assure proper disposal of smaller empty containers, consult with state and local regulations and disposal authorities.
Page 13 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS
* * * Section 14 – TRANSPORTATION INFORMATION * * * DOT Information Shipping Name: Petroleum Products, n.o.s. (condensate) UN #: 1268 Hazard Class: 3 Additional Info.: Dependent on the product’s properties, the shipper may also elect to
classify as Gasoline UN1203 or Petroleum Crude Oil UN1267 - reference 49 CFR 172.101 for further description (e.g., packing group determination).
Placard:
* * * Section 15 – REGULATORY INFORMATION * * * Regulatory Information Component Analysis This material contains one or more of the following chemicals required to be identified
under SARA Section 302 (40 CFR 355 Appendix A), SARA Section 313 (40 CFR 372.65) and/or CERCLA (40 CFR 302.4).
Benzene (71-43-2) SARA 313: 0.1% de minimis concentration CERCLA: 10 lb final RQ (received an adjusted RQ of 10 lbs based on
potential carcinogenicity in an August 14, 1989 final rule); 4.54 kg final RQ (received an adjusted RQ of 10 lbs based on potential carcinogenicity in an August 14, 1989 final rule)
SARA Section 311/312 – Hazard Classes Acute Health Chronic Health Fire Sudden Release of Pressure Reactive X X X -- -- SARA SECTION 313 – SUPPLIER NOTIFICATION This product contains the following toxic chemicals subject to the reporting requirements
of section 313 of the Emergency Planning and Community Right-To-Know Act (EPCRA) of 1986 and of 40 CFR 372:
Page 14 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS INGREDIENT NAME (CAS NUMBER) CONCENTRATION PERCENT BY WEIGHT Benzene (71-43-2) <0.1 to 2 Canadian Regulatory Information DSL/NDSL
Inventory This product has been classified in accordance with the hazard criteria of the Controlled Products Regulations (CPR) and the SDS contains all the information required by the Regulations.
Workplace Hazardous Materials Information System
B2 - Flammable Liquid D1A – Material Causing Immediate and Serious Toxic Effects - Very Toxic Material D2A: Material Causing Other Toxic Effects Very Toxic D2B - Material Causing Other Toxic Effects - Toxic Material
European Union Regulatory Information
Labeling Product is dangerous as defined by the European Union Dangerous Substances / Preparations Directives. Contains: Low Boiling Point Naphtha
Symbol F+ Extremely Flammable T Toxic N Dangerous for the Environment
Risk Phrases
R12-45-38-65-67-51/53 Extremely flammable. May cause cancer. Irritating to skin. Harmful: may cause lung damage if swallowed. Vapors may cause drowsiness and dizziness. Toxic to aquatic organisms, may cause long-term adverse effects in the aquatic environment.
Safety Phrases
S16-53-45-2-23-24-29-43-62 Keep away from sources of ignition – No smoking. Avoid exposure – obtain special instructions before use. In case of accident or if you feel unwell, seek medical advice immediately (show the label where possible). Keep out of reach of children. Do not breathe vapor. Avoid contact with skin. Do not empty into drains. In case of fire use foam/dry powder/CO2. If swallowed, do not induce vomiting: seek medical advice immediately and show this container or label.
Page 15 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS State Regulations Component Analysis – State The following components appear on one or more of the following state hazardous
substances lists
Component CAS CA MA MN NJ PA RI Octanes 111-65-9 Yes No Yes Yes Yes Yes
Heptanes 142-82-5 Yes No Yes Yes Yes Yes
n-Hexane 110-54-3 Yes Yes Yes Yes Yes Yes
n-Pentane 109-66-0 Yes No Yes Yes Yes Yes
n-Butane 106-97-8 Yes No Yes Yes Yes Yes
Propane 74-98-6 No No Yes Yes Yes Yes
Ethane 78-84-0 No No Yes Yes Yes No
Benzene 71-43-2 Yes Yes Yes Yes Yes Yes
Toluene 108-88-3 Yes Yes Yes Yes Yes Yes
m-, o-, p-Xylene 1330-20-7 Yes Yes Yes Yes Yes Yes
The following statement(s) are provided under the California Safe Drinking Water and Toxic Enforcement Act of 1986 (Proposition 65): WARNING! This product contains a chemical known to the state of California to cause cancer. WARNING! This product contains a chemical known to the state of California to cause Reproductive / developmental effects. Component Analysis – WHMIS IDL The following components are identified under the Canadian Hazardous Products Act Ingredient Disclosure List: Component CAS # Minimum Concentration Benzene 71-43-2 0.1%
* * * Section 16 – OTHER INFORMATION * * *
NFPA® Hazard Rating Health 1 Fire 4 Reactivity 0 HMIS® Hazard Rating Health 1 Slight Fire 4 Severe Physical 0 Minimal * Chronic
1 4
0
Page 16 of 17
SAFETY DATA SHEET
Material Name: Natural Gas Condensate US GHS Key/Legend EPA = Environmental Protection Agency; TSCA = Toxic Substance Control Act: ACGIH =
American Conference of Governmental Industrial Hygienists; IARC = International Agency for Research on Cancer; NIOSH = National Institute for Occupational Safety and Health; NTP = National Toxicology Program; OSHA = Occupational Safety and Health Administration; NJTSR = New Jersey Trade Secret Registry.
Literature References None Other Information The information presented herein has been compiled from sources considered to be
dependable, and is accurate and reliable to the best of our knowledge and belief, but is not guaranteed to be so. Since conditions of use are beyond our control, we make no warranties, expressed or implied, except those that may be contained in our written
contract of sale or acknowledgment. Vendor assumes no responsibility for injury to vendee or third persons proximately
caused by the material if reasonable safety procedures are not adhered to as stipulated in the data sheet. Additionally, vendor assumes no responsibility for injury to vendee or third persons proximately caused by abnormal use of the material, even if reasonable safety procedures are followed. Furthermore, vendee assumes the risk in their use of the material.
Date of Preparation: January 29, 2014 Date of Last Revision: March 4, 2014
End of Sheet
Page 17 of 17
SAFETY DATA SHEET
Material Name: Produced Water US GHS SYNONYMS: Produced Brine Water, Brine, Brine Water, Formation Water
* * * Section 1 – PRODUCT AND COMPANY IDENTIFICATION * * * PRODUCT NAME: Produced Water EMERGENCY PHONE: (800) 878-1373 PRODUCT CODES: Mixture AFTER HOURS: (800) 878-1373 PRODUCER: Antero Resources ADDRESS: 1615 Wynkoop Street CHEMTREC PHONE: (800) 424-9300 Denver, Colorado 80202
* * * Section 2 – HAZARDS IDENTIFICATION * * * GHS Classification: Eye Irritant – Category 2A. GHS LABEL ELEMENTS Symbol(s)
Signal Word Warning Hazard Statements Causes serious eye irritation Precautionary Statements Prevention Wear protective gloves/protective clothing/eye protection/face protection. Response If on SKIN (or hair): Rinse skin with water / shower. Remove / Take off all
contaminated clothing immediately.
Page 1 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
If in EYES: Rinse cautiously with water for at least fifteen (15) minutes. Remove Contact Lenses, if present and easy to do. Continue rinsing. If EYE irritation persists, get medical advice / attention. Storage Store in a secure area. Disposal Dispose of contents/containers in accordance with
regulations.
* * * Section 3 – COMPOSITION / INFORMATION ON INGREDIENTS * * *
CAS # Component Percent 7732-18-5 Water 80 7647-14-5 Sodium Chloride 20
Because brine water is a natural product, composition can vary greatly.
* * * Section 4 – FIRST AID MEASURES * * *
First Aid: Eyes Flush eyes with clean running water for at least fifteen (15) minutes. If irritation
or redness develops from exposure, following flushing, seek medical attention. First Aid: Skin First aid is not required, normally. However, it is a good practice to wash any
chemical from the skin.
First Aid: Ingestion (Swallowing) First aid is not required, normally. If spontaneous vomiting occurs, lean the
victim forward to reduce the risk of aspiration. Monitor for breathing difficulties. If symptoms develop, seek medical attention.
First Aid: Inhalation (Breathing) Remove person to fresh air. If person is not breathing, provide artificial
respiration. If necessary, provide additional oxygen once breathing is restored if trained to do so. Seek medical attention immediately.
Page 2 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
Most important symptoms and effects None known or anticipated.
* * * Section 5 – FIRE FIGHTING MEASURES * * * NFPA 704 Hazard Class Health: 1 Flammability: 0 Instability: 0 (0=Minimal, 1=Slight, 2=Moderate, 3=Serious, 4=Severe) General Fire Hazards No fire hazards are expected. General Fire Hazards No unusual fire or explosion hazards are expected. If container is not properly
cooled, it can rupture in the heat of a fire.
Extinguishing Media The material is non-flammable. Use extinguishing agent suitable for the type of
surrounding fire.
Unsuitable Extinguishing Media None
Fire Fighting Equipment / Instructions Small fires in the beginning stage may typically be extinguished using handheld portable fire extinguishers and other firefighting equipment. Isolate area around container involved in fire and keep unauthorized personnel out. Stop spill/release if it can be done safely. Move undamaged containers from the immediate hazard area if it can be done safely. Cool equipment exposed to fire with water, if it can be done safely. Hazardous Combustion Products None Anticipated. See Section 9 for Flammable Properties including Flash Point and Flammable (Explosive) Limits
0 1 0
Page 3 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
* * * Section 6 – ACCIDENTAL RELEASE MEASURES * * *
Recovery and Neutralization Contain and stop the source of the spill, if safe to do so.
Materials and Methods for Clean-Up Notify relevant authorities in accordance with all applicable regulations.
Immediate cleanup of any spill is recommended. Dike far ahead of spill for later recovery or disposal. Absorb spill with inert material such as sand or vermiculite, and place in suitable container for disposal. If spilled on water remove with appropriate methods (e.g. skimming, booms or absorbents). In case of soil contamination, remove contaminated soil for remediation or disposal, in accordance with local regulations.
Recommended measures are based on the most likely spillage scenarios of this
material. However, local conditions and regulations may influence or limit the choice of appropriate actions to be taken. See Section 13 for information on appropriate disposal.
Emergency Measures The material is not considered hazardous. Nevertheless, evacuate nonessential
personnel and secure the area. Stay upwind and uphill, if possible. Personal Precautions and Protective Equipment Stay upwind and away from the spill/release. Avoid direct contact with the
material. For large spillages, notify persons downstream of the spill/release. Isolate the immediate hazard area and keep unauthorized personnel out. Response and clean-up crews must be properly trained and must utilize proper protective equipment (see Section 8).
Environmental Precautions Protect bodies of water by diking or absorbents, if possible. Do not flush down
sewer or drainage systems. Use water sparingly to minimize environmental contamination and reduce disposal requirements. If a spill occurs on water, notify appropriate authorities and advise shipping of any hazard.
Prevention of Secondary Hazards None
Page 4 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
* * * Section 7 – HANDLING AND STORAGE * * *
Handling Procedures Wash thoroughly after handling. Use good personal hygiene practices and wear
appropriate personal protective equipment (see section 8). Do not enter confined spaces such as tanks or pits without following proper
entry procedures such as ASTM D-4276 and 29 CFR 1910.146. Do not wear contaminated clothing or shoes.
Storage Procedures Keep container(s) tightly closed and properly labeled. Use and store this
material in cool, dry, well ventilated areas. Store only in approved containers. Keep away from any incompatible material (see Section 10). Protect container(s) against physical damage.
Incompatibilities Keep away from excessive heat to prevent rupture of container.
* * * Section 8 – EXPOSURE CONTROLS / PERSONAL PROTECTION * * * Component Exposure Limits Water (7732-18-5) ACGIH: Not listed Sodium Chloride (7647-14-5) ACGIH: Not listed Engineering Measures If current ventilation practices are not adequate to maintain airborne
concentrations below the established exposure limits, additional engineering controls may be required.
Personal Protective Equipment: Respiratory Emergencies or conditions that could result in significant airborne exposures
may require the use of NIOSH approved respiratory protection. An industrial hygienist or other appropriate health and safety professional should be consulted for specific guidance under these situations.
A respiratory protection program that meets or is equivalent to OSHA 29 CFR
Page 5 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
1910.134 and ANSI Z88.2 should be followed whenever workplace conditions warrant a respirator's use.
Personal Protective Equipment: Skin and Hands The use of skin protection is not normally required; however, good industrial
hygiene practice suggests the use of gloves or other appropriate skin protection whenever working with chemicals.
Personal Protective Equipment: Eyes Safety glasses or goggles that meet or exceed ANSI Z-87.1 are recommended
where there is a possibility of splashing or spraying. Hygiene Measures Emergency eye wash capability should be available in the near proximity to
operations presenting a potential splash exposure. Use good personal hygiene practices. Avoid repeated and/or prolonged skin exposure. Wash hands before eating, drinking, smoking, or using toilet facilities. Promptly remove contaminated clothing and launder before reuse.
* * * Section 9 – PHYSICAL AND CHEMICAL PROPERTIES * * * Appearance: Clear to Brown Odor: Salty
Physical State: Liquid pH: ND
Vapor Pressure: < 0.36 psia @ 70°F /
21.1°C Vapor Density: > 1
Boiling Point: 212°F / 100°C Melting Point: 2.4°F / -16.5°C Solubility (H2O): Complete Specific Gravity: 1.1 @ 68°F / 20°C Evaporation Rate: Variable VOC: ND Octanol / H2O
Coeff.: ND Flash Point: ND
Flash Point Method:
ND
Lower Flammability Limit:
ND Upper Flammability Limit: ND
(LFL): (UFL): Auto Ignition: ND Burning Rate: ND
Page 6 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
* * * Section 10 – CHEMICAL STABILITY & REACTIVITY INFORMATION * * *
Chemical Stability This is a stable material.
Hazardous Reaction Potential Will react with alkali and alkaline metals to form flammable hydrogen gas. Conditions to Avoid Avoid contact with alkali metals (lithium, sodium, potassium), alkaline metals
(beryllium, magnesium, calcium, strontium, and barium), and metallic hydrides like lithium aluminum hydride.
Hazardous Decomposition Products Not anticipated under normal conditions of use. Hazardous Polymerization Not known to occur.
* * * Section 11 – TOXICOLOGICAL INFORMATION * * * Acute Toxicity A: General Product Information Unlikely to be harmful. B. Component Analysis – D50/LC50 Water (7732-18-5) Oral LD50 Rat 90 g/kg Sodium Chloride (7647-14-5) Oral LD50 Rat 3 g/kg Potential Health Effects: Skin Corrosion Property / Stimulativeness May cause skin irritation with prolonged or repeated contact. Not expected to be
a skin sensitizer. Potential Health Effects: Eye Critical Damage / Stimulativeness Contact with eyes may cause moderate irritation.
Page 7 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
Potential Health Effects: Ingestion Ingestion may result in nausea, vomiting, diarrhea, abdominal cramps, and
dehydration (thirst). Potential Health Effects: Inhalation No information available on the mixture. However, none of the components
have been classified for respiratory sensitization (or are below the concentration threshold for classification).
Generative Cell Mutagenicity Not expected to cause genetic effects. Carcinogenicity General Product Information Not expected to cause cancer. This substance is not listed as a carcinogen by
IARC, NTP or OSHA. Reproductive Toxicity This product is not reported to have any reproductive toxicity effects. Specified Target Organ General Toxicity: Single Exposure This product is not reported to have any specific target organ general toxicity
single exposure effects. Specified Target Organ General Toxicity: Repeated Exposure This product is not reported to have any specific target organ general toxicity
multiple exposure effects. Aspiration Respiratory Organs Hazard The major health threat of ingestion occurs from the danger of aspiration
(breathing) of liquid drops into the lungs, particularly from vomiting. Aspiration may result in chemical pneumonia (fluid in the lungs), severe lung damage, respiratory failure and even death.
* * * Section 12 – ECOLOGICAL INFORMATION * * * Ecotoxicity A: General Product Information Keep out of sewers, drainage areas, and waterways. Report spills and
releases, as applicable under Federal and State regulations.
Page 8 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
Persistence / Degradability No information available Bioaccumulation No information available Mobility in Soil No information available
* * * Section 13 – DISPOSAL CONSIDERATIONS * * * Waste Disposal Instructions See Section 7 for Handling Procedures. See Section 8 for Personal Protective
Equipment Recommendations. Disposal of Contaminated Containers or Packaging Recover or recycle if possible. It is the responsibility of the generator to
determine the toxicity and physical properties of the material generated so as to properly classify the waste and ensure disposal methods comply with applicable regulations.
This material, if discarded as produced, is not a RCRA "listed" hazardous waste, and is not believed to exhibit characteristics of hazardous waste. Consult state and local regulations regarding the proper disposal of this material. Do not dispose of brine water by draining onto the ground. This will result in soil and groundwater contamination. Waste arising from spillage or tank cleaning should be disposed of in accordance with applicable regulations.
Container contents should be completely used and containers should be emptied prior to discard. Container rinsate should not be considered a RCRA hazardous waste but must be disposed of with care and in full compliance with federal, state and local regulations. Larger empty containers, such as drums, should be returned to the distributor or to a qualified drum reconditioner. To assure proper disposal of smaller empty containers, consult with state and local regulations and disposal authorities.
* * * Section 14 – TRANSPORTATION INFORMATION * * * DOT Information Shipping Description: Not Regulated UN #: Not Regulated
Page 9 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
* * * Section 15 – REGULATORY INFORMATION * * *
CERCLA/SARA – Section 302 Extremely Hazardous Substances and TPQs (in
pounds): This material does not contain any chemicals subject to the reporting requirements of SARA 302 and 40 CFR 372, CERCLA/SARA – Section 313 and 40 CFR 372): This material does not contain any chemicals subject to the reporting requirements of SARA 313 and 40 CFR 372. EPA (CERCLA) Reportable Quantity (in pounds): This material does not contain any chemicals with CERCLA Reportable Quantities. State Regulations Component Analysis
The following components appear on one or more of the following state hazardous substances list.
California Proposition 65: This material does not contain any chemicals that are known to the State of California to cause cancer, birth defects or other reproductive harm at concentrations that trigger the warning requirements of California Proposition 65. National Chemical Inventories: All components are either listed on the US TSCA Inventory, or are not regulated under
TSCA. U.S. Export control classification Number: EAR99.
* * * Section 16 – OTHER INFORMATION * * *
NFPA® Hazard Rating Health 1 Fire 0 Reactivity0 HMIS® Hazard Rating Health 1 Slight Fire 0 Minimal Physical 0 Minimal
Page 10 of 11
SAFETY DATA SHEET
Material Name: Produced Water US GHS
Key/Legend EPA = Environmental Protection Agency; TSCA = Toxic Substance Control Act: ACGIH
= American Conference of Governmental Industrial Hygienists; IARC = International Agency for Research on Cancer; NIOSH = National Institute for Occupational Safety and Health; NTP = National Toxicology Program; OSHA = Occupational Safety and Health Administration; NJTSR = New Jersey Trade Secret Registry.
Literature References None Other Information The information presented herein has been compiled from sources considered
to be dependable, and is accurate and reliable to the best of our knowledge and belief, but is not guaranteed to be so. Since conditions of use are beyond our control, we make no warranties, expressed or implied, except those that may be contained in our written contract of sale or acknowledgment.
Vendor assumes no responsibility for injury to vendee or third persons
proximately caused by the material if reasonable safety procedures are not adhered to as stipulated in the data sheet. Additionally, vendor assumes no responsibility for injury to vendee or third persons proximately caused by abnormal use of the material, even if reasonable safety procedures are followed. Furthermore, vendee assumes the risk in their use of the material.
Date of Preparation: January 28, 2014 Date of Last Revision: March 4, 2014
End of Sheet
Page 11 of 11
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment O
Emissions Summary Sheet
Source Device
Type
lb/hr ton/yr lb/hr
1.01 4.43 1.01
1.20 5.27 1.20
1451.97 6359.64 1451.97
0.01 0.03 0.01
0.09 0.40 0.09
0.02 0.09 0.02
0.07 0.29 0.07
0.00 0.01 0.00
0.02 0.08 0.02
0.03 0.14 0.03
0.20 0.87 0.20
0.07 0.32 0.07
80.94 354.50 80.94
3.79 16.59 3.79
0.00 0.01 0.00
6.28 5.51 6.28
0.01 0.01 0.01
3.23 12.36 3.23
EP-HR001 Haul Truck 1.33 8.37 0.66 MB
0.00 0.00 0.44
0.00 0.00 0.53
1761.44 7715.13 2679.58
0.00 0.00 0.04
0.21 0.91 0.00
0.46 2.00 0.01
0.27 1.18 0.01
5.58 24.45 0.11
0.49 2.13 0.01
280.21 1227.31 5.60
0.01 0.06 0.01
9.03 39.56 9.03
0.11 0.50 0.11
5.64 24.72 5.64
0.32 1.38 0.32
27.78 121.66 27.78
0.00 0.01 0.00
0.00 0.02 0.00
0.01 0.03 0.01
Table 1: Emissions Data
24.72
1.38
121.66
0.01
CO (630080)
NOx (10102439)
CO2 EquivalentN2O (10024972), CO2 (124389), CH4
(74828)
MBGas/Vapor/
Solid (for PM)
EP-ENG001 Vertical Stack
ID No. ID No.
F001 n/a F001
ENG001 Compressor
Engine
N/A
0.02
0.03Total VOCs
TAPs Formaldehyde (50000)
CO (630080)
NOx (10102439)
Gas/Vapor
PM, PM10, PM2.5
MB
Emission Point ID No.
(Must match Emission
Units Table
& Plot Plan)
Emission Point
Type1
Emission Unit Vented
Through This Point
(Must match Emission Units
Table & Plot Plan)
Air Pollution Control
Device (Must match
Emission Units Table &
Plot Plan)
All Regulated Pollutants
- Chemical Name/CAS3
(Speciate VOCs
& HAPS)
Maximum Potential
Uncontrolled Emissions 4
Maximum Potential
Controlled Emissions 5
Emission Form
or Phase
(At exit
conditions, Solid,
Liquid or
Gas/Vapor)
Est.
Method
Used 6
Fugitives
Gas/Vapor
/Solid (for PM)
4.43
5.51
0.03
NOx (10102439)
CO2 EquivalentN2O (10024972), CO2 (124389), CH4
(74828)
SO2 (7446095)
0.40
0.09
PM, PM10, PM2.5
Hexane (110543)
Gas/Vapor
ton/yr
Total VOCs
Toluene (108883)
Ethyl benzene (100414)
Hexane (110543)
Benzene (71432)
CO (630080)
5.27
6359.64
N/A
0.01
0.01
0.08
0.14
0.87
0.32
16.59
o,m,p-xylenes
(95476,108383,106423)
CO2 EquivalentCO2 (124389)), CH4
VOCs
TAPs (benzene)
n/a HR001 N/A PM, PM10, PM2.5
1.94Condensate
Tanks, PW
Tanks, and
Enclosed
Combustor
N/A
EP-L001, EP-L002 n/a L001, L002 Loading
(Condensate),
Loading (Water)
N/A Gas/Vapor
hexane (110543)
VOCs
CO2 EquivalentCO2 (124389), CH4
0.01
12.36
Enclosed
Combustor
Benzene (71432)
Toluene (108883)
hexane (110543)
VOCs
MB
0.49
MB
11736.54
0.18
4.19
24.55
Gas/Vapor/
Solid (for PM)
0.04
Solid
0.02
PM, PM10, PM2.5
2.31
ethyl benzene (100414)
o,m,p-xylenes
(95476,108383,106423)
0.02
0.04
0.29
EP-H001, EP-H002, EP-
H003, EP-H004, EP-
H005, EP-H006, EP-
H007, EP-H008, EP-
H009, EP-H010
Vertical Stack H001, H002,
H003, H004,
H005, H006,
H007, H008,
H009, H010
Gas Production
Unit Heater
N/A
EP-PCV valve PCV Pneumatic CV N/A MB
EP-EC001 n/a TANKCOND001-
010,
TANKPW001-
002, and EC001 CO2 EquivalentN2O (10024972), CO2 (124389), CH4
Attachment O: G70-A Emissions Summary Sheet
Emission Points Data Summary Sheet
MB
AP-42
354.50
0.06
39.56
0.50
hexane (110543)
CO2 EquivalentCO2 (124389)), CH4
VOCs
lb/hr lb/hr ton/yr
Haul Road/Road Dust Emissions
Paved Haul Roads
n/a
Unpaved Haul Roads PM, PM10, PM2.5 1.3291 0.6645 4.1859 MB
VOCs 6.2848 6.2848 5.5080
toluene (108883) 0.0009 0.0009 0.0008
ethyl benzene (100414) 0.0010 0.0010 0.0009
hexane (110543) 0.0086 0.0086 0.0075
o,m,p-xylenes (95476,108383,106423) 0.0022 0.0022 0.0019
CO2 Equivalent
CO2 (124389), CH43.2288 3.2288 12.3613
benzene (71432) 0.0002 0.0002 0.0002
TAPs (benzene) 0.0002 0.0002 0.0002
Benzene (71432) 0.0103
Toluene (108883) 0.0788
Ethyl benzene (100414) 0.1384
Hexane (110543) 0.8741
o,m,p-xylenes (95476,108383,106423) 0.3209
CO2 Equivalent
CO2 (124389)), CH4354.4988
VOCs 16.5870
TAPs (benzene) 0.0103
toluene (108883) 0.00E+00 0.00E+00 0.00E+00
ethyl benzene (100414) 0.00E+00 0.00E+00 0.00E+00
hexane (110543) 0.0136 0.0136 0.0596
o,m,p-xylenes (95476,108383,106423) 0.00E+00 0.00E+00 0.00E+00
CO2 Equivalent
CO2 (124389)), CH49.0327 9.0327 39.5633
VOCs 0.1145 0.1145 0.5015
TAPs (benzene) 0.00E+00 0.00E+00 0.00E+00
2 Give rate with no control equipment operating. If emissions occur for less than 1 hr, then record emissions per batch in minutes (e.g. 5 lb VOC/20 minute batch).
3 Give rate with proposed control equipment operating. If emissions occur for less than 1 hr, then record emissions per batch in minutes (e.g. 5 lb VOC/20 minute batch).
4 Indicate method used to determine emission rate as follows: MB = material balance; ST = stack test (give date of test); EE = engineering estimate; O = other
(specify).
FUGITIVE EMISSIONS SUMMARYAll Regulated Pollutants
Chemical Name/CAS 1
Maximum Potential
Uncontrolled Emissions 2
Maximum Potential
Controlled Emissions 3
0.0103
Est.
Method
Used 4ton/yr
8.3718
5.5080
0.00E+00
MB
Loading/Unloading Operations
0.0008
0.0009
0.0075
0.0019
12.3613
0.0002
0.0002
MB
354.4988
16.5870
0.0103
Does not apply Does not apply
Attachment C/O: G70-A Emissions Summary SheetFugitive Emissions Data Summary Sheet
1 List all regulated air pollutants. Speciate VOCs, including all HAPs. Follow chemical name with Chemical Abstracts Service (CAS) number. LIST Acids, CO, CS2, VOCs, H2S, Inorganics,
Lead, Organics, O3, NO, NO2, SO2, SO3, all applicable Greenhouse Gases (including CO2 and methane), etc. DO NOT LIST H2, H2O, N2, O2, and Noble Gases.
Equipment Leaks (Components)
0.00E+00
0.00E+00
0.0596
0.00E+00
Equipment Leaks (PCVs)
MB
0.0788
0.1384
0.8741
0.3209
39.5633
0.5015
Antero Resources Corporation General Permit Application G70-A Edna Monroe Well Pad
082715 (197)
May 2015
Attachment P
Other Supporting Documentation
(Engine EPA’s Certificate of Conformity and Technical Information)
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY2013 MODEL YEAR
CERTIFICATE OF CONFORMITYWITH THE CLEAN AIR ACT OF 1990
OFFICE OF TRANSPORTATIONAND AIR QUALITY
ANN ARBOR, MICHIGAN 48105
Certificate Issued To: Kubota Corporation (U.S. Manufacturer or Importer)
Certificate Number: DKBXS.9622HP-002
Effective Date:11/20/2012
Expiration Date:12/31/2013
_________________________Byron J. Bunker, Division Director
Compliance Division
Issue Date:11/20/2012
Revision Date:N/A
Manufacturer: Kubota CorporationEngine Family: DKBXS.9622HPCertificate Number: DKBXS.9622HP-002Useful Life : 1000 Hours / 5 YearsEngine Class : Nonhandheld-Class IIFuel : Natural Gas (CNG/LNG)Emission Standards : NMHC + NOx ( g/kW-hr ) : 8 CO ( g/kW-hr ) : 610
Pursuant to Section 213 of the Clean Air Act (42 U.S.C. section 7547), 40 CFR Part 1054, 40 CFR Part 1068 and 40 CFR Part 60 (stationary only and combined stationary and mobile), and subject to theterms and conditions prescribed in those provisions, this certificate of conformity is hereby issued for the following small nonroad engine family, more fully described in the documentation required by 40CFR Part 1054 and produced in the stated model year.
This certificate of conformity covers only those new small nonroad engines which conform in all material respects to the design specifications that applied to those engines described in the documentationrequired by 40 CFR Part 1054 and which are produced during the model year stated on this certificate of the said manufacturer, as defined in 40 CFR Part 1054. This certificate of conformity does not coversmall nonroad engines imported prior to the effective date of the certificate.
It is a term of this certificate that the manufacturer shall consent to all inspections described in 40 CFR 1068.20 and 1068, Subpart E and authorized in a warrant or court order. Failure to comply with therequirements of such a warrant or court order may lead to revocation or suspension of this certificate for reasons specified in 40 CFR Part 1054. It is also a term of this certificate that this certificate may berevoked or suspended or rendered void ab initio for other reasons specified in 40 CFR Part 1054, 40 CFR Part 1068.
This certificate does not cover small nonroad engines sold, offered for sale, or introduced, or delivered for introduction, into commerce in the U.S. prior to the effective date of the certificate.
TECHNICAL INFORMATION
DG972-SAEH-S1
NATURAL GAS FUEL ENGINE
July, 2006
KUBOTA Corporation
CONTENTS
1. GENERAL SPECIFICATIONS
2. PERFORMANCE CURVES
3. DIMENSIONS
4. TECHNICAL DATA
4-1) BRAKE HORSE POWER
4-2) FUEL CONSUMPTION
4-3) NOISE LEVEL
4-4) AIR REQUIREMENTS
1. Combustion air requirements
2. Cooling air requirements
3. Combustion and cooling air requirements
4-5) EXHAUST GAS VOLUME
4-6) HEAT REJECTION TO COOLING WATER (Ho)
4-7) COOLING FAN DATA
4-8) CENTER OF GRAVITY
4-9) UNBALANCED FORCES OF ENGINES
4-10) MASS ELASTIC SYSTEM
5. FUEL SYSTEM AND FUEL DIAGRAM Specifications and dimensions are subject to change without prior notice.
1. GENERAL SPECIFICATIONS ITEM UNIT SPECIFICATIONS
Engine model DG972-SAEH-S1
Type Vertical, In line, 4cycle Natural Gas engine
Cooling system Water cooling with water pump Number of cylinders 3 Cylinder bore mm(in) 74.5 (2.93) Stroke mm(in) 73.6 (2.90) Total displacement L(cu. in) 0.962 (58.7) High idle rpm 3850 Low idle rpm 1500 Horsepower kW(HP) 19.5(26.1) Max. torque (SAE J1349)
Nm(ft-lb) /rpm 61.2 (45.2)/2400
Compression ratio 9.2 Firing order 1-2-3 Ignition timing B.T.D.C.15°/1000rpm B.T.D.C.28°/3600rpm Ignition system Distributor-less Solid State type Fuel Natural Gas only Direction of rotation Counter-clockwise from flywheel side Starting system Electric starting with cell starter Starter output V-kW 12-1.0 Alternator output V-W 12-480 (Standard) Lubricating system Forced lubricating by trochoid pump Lubricating oil Quality better than SH class Lube. oil capacity L(US gal) 3.4 (0.90) Coolant capacity L(US gal) 1.22 (0.32) Governor type Centrifugal flyweight mechanical type governor Dimensions (LxBxH) mm(in) 526x415x503 (20.7x16.3x19.8) Dry weight kg(lb) Approx. 95.4(210) Application Stationary only
2. PERFORMANCE CURVES
DG972 PERFORMANCE CURVES Higher calorific value : 11000kcal/m3 (1236BTU/ft3)
3. DIMENSIONS
4. TECHNICAL DATA ITEM SPECIFICATIONS
Engine model DG972-SAEH-S1 Brake horse power See attached sheet 4-1)Top Clearance 1.35 to 1.65mm (0.05315 to 0.06496in) Compression pressure 1.32MPa (192psi) Fuel consumption See attached sheet 4-2)Lube. oil consumption Max.0.67g/kWh (0.5g/HPh) at rated load
at idling speed: more than 69kPa (more than 9.95psi) Lube. oil pressure
at rated speed: 196 to 441kPa (28.44 to 63.99psi) Noise level See attached sheet 4-3)Combustion air requirements Cooling air requirements Combustion and cooling air requirements
See attached sheet (Refer to 25deg.C and 1000hPa) 4-4)
Exhaust gas volume See attached sheet (Refer to 25deg.C and 1000hPa) 4-5)
Cold starting limits -15deg.C (5deg.F) Heat rejection See attached sheet 4-6)
30° (Less than 10min. continuous operation) Front or Rear down 20° (Continuous operation)
30° (Less than 10min. continuous operation) Angles of tilt Left or Right
side down 20° (Continuous operation)
[Inlet valve] Open: TDC –20° Close: BDT +45° Valve timing
[Exhaust valve] Open: BDC –50° Close: TDC +15° Cooling fan data See attached sheet 4-7)Center of gravity See attached sheet 4-8)Unbalanced forces of engines See attached sheet 4-9)Mass elastic system See attached sheet 4-10)
Opening temperature: 71±1.5deg.C (159.8±2.7deg.F) Thermostat specifications Fully opened temperature: 85deg.C (185deg.F)
[at Thermostat lift:8mm (0.31in)]
4-1) BRAKE HORSE POWER SAE J1349
Engine speed rpm 2000 2400 2800 3200 3600 kW 12.6 15.4 17.4 18.9 19.5 HP 16.9 20.6 23.3 25.3 26.1
Net intermittent
PS 17.1 20.9 23.7 25.7 26.5 kW 10.1 12.3 13.9 15.1 15.6 HP 13.5 16.5 18.7 20.3 20.9
Net continuous
PS 13.7 16.8 18.9 20.6 21.2 Note 1. Conversion rates 1kW=1.35962PS=1.34048HP
1PS=0.7355kW=0.985925HP 1HP=0.7457kW=1.01428PS
2. Fuel detail Japanese standard gas higher calorific value : 11000kcal/m3 (1236BTU/ft3) supply pressure : 0.98 – 2.45kPa (7.35 – 18.38mmHg)
4-2) FUEL CONSUMPTION Specific at net intermittent (SAE J1349)
Engine speed rpm 2000 2400 2800 3200 3600 kW 12.6 15.4 17.4 18.9 19.5 HP 16.9 20.6 23.3 25.3 26.1 Brake horse power PS 17.1 20.9 23.7 25.7 26.5
g/kWh 269 264 269 273 273 g/HPh 200 197 200 204 204 g/PSh 198 194 198 201 201 Fuel consumption
lb/HPh 0.442 0.434 0.442 0.449 0.449 Note 1. Conversion rates 1kW=1.35962PS=1.34048HP 1kg=2.20462lb (1g=0.00220462lb)
1PS=0.7355kW=0.985925HP 1lb=0.45359kg 1HP=0.7457kW=1.01428PS
2. Fuel detail Japanese standard gas higher calorific value : 11000kcal/m3 (1236BTU/ft3) supply pressure : 0.98 – 2.45kPa (7.35 – 18.38mmHg)
4-3) NOISE LEVEL Load×rpm Unit Sound pressure at 1m(3.3ft) 0/4×3850 dB(A) 90.0 4/4×3850
15.6kW (20.9HP) dB(A) 92.0
0/4×1500 dB(A) 72.0 These data show the average noise level at four points. Note 1. Measurement conditions: With radiator, cooling fan, air cleaner and muffler.
4-4) AIR REQUIREMENTS 1. Combustion air requirements (Refer to 25deg.C and 1000hPa)
rpm 2000 2400 2800 3200 3600 L/sec 12.35 14.81 17.28 19.75 22.22 m3/h 44.44 53.33 62.22 71.11 80.00
in3/sec 753 904 1055 1205 1356 ft3/min 26.13 31.35 36.58 41.80 47.03
Combustion air requirements calculating formula Q1=Vh•N•C•η•10-3
Q1: Amount of intake air (m3/min) η: Intake efficiency Vh: Total displacement (L) Natural Gas: 0.77 N: Engine speed (rpm) C: Coefficient=0.5
2. Cooling air requirements (Refer to 25deg.C and 1000hPa) rpm 2000 2400 2800 3200 3600
L/sec 571.2 737.2 824.7 833.9 764.7 m3/h 2056 2654 2969 3002 2753
in3/sec 34859 44984 50327 50888 46667 ft3/min 1210.2 1561.8 1747.3 1766.7 1620.2
Above data is decided by following conditions.
1. Using the standard radiator. 2. Engine is run as open unit.
3. Combustion and cooling air requirements (Refer to 25deg.C and 1000hPa) rpm 2000 2400 2800 3200 3600
L/sec 583.5 752.0 842.0 853.7 786.9 m3/h 2100.4 2707.3 3031.2 3073.1 2833.0
in3/sec 35612 45888 51382 52093 48023
ft3/min 1236.3 1593.2 1783.9 1808.5 1667.2
Note 1. Cooling fan and fan pulley specifications(Cooling fan Part No. 15881-74112)
Item Fan diameter 300mm (11.81in) No. of blade and type of shape 4, S type Diameter of fan driving pulley 100mm (3.94in) Diameter of fan pulley 84mm (3.31in) 2. Conversion rates
1L=61.0237in3=0.035315ft3 1ft3=28.3168L 1L/sec=3.6m3/h=2.1189ft3/min
4-5) EXHAUST GAS VOLUME Refer to 25deg.C and 1000hPa
rpm 2000 2400 2800 3200 3600 L/sec 35.46 42.55 49.65 56.74 63.83 m3/h 127.67 153.19 178.73 204.26 229.80
in3/sec 2164 2597 3030 3462 3895 ft3/min 75.05 90.06 105.07 120.08 135.09
Note 1. Conversion rates 1L=61.0237in3=0.035315ft3
1ft3=28.3168L 1L/sec=3.6m3/h=127.133ft3/hr
4-6) HEAT REJECTION TO COOLING WATER 1. Specific at net intermittent (SAE J1349)
Engine speed rpm 2000 2400 2800 3200 3600 kW 12.6 15.4 17.4 18.9 19.5 HP 16.9 20.6 23.3 25.3 26.1 Brake horse power PS 17.1 20.9 23.7 25.7 26.5
g/kWh 269 264 269 273 273 g/HPh 200 197 200 204 204 g/PSh 198 194 198 201 201 Fuel consumption
lb/HPh 0.442 0.434 0.442 0.449 0.449 MJ/h 29.05 31.52 38.79 45.13 51.82 kcal/h 6940 7529 9267 10781 12379 Heat rejection to
cooling water BTU/h 12491 13551 16679 19404 22281 Note Heat rejection to cooling water calculating formula Ho=Hu•Ne•be•i
Ho: Heat rejection to cooling water Hu: Fuel low calorific value Japanese standard gas; 49.4MJ/kg, 11800kcal/h, 212391BTU/lb Ne: Brake horse power Be: Specific fuel consumption
i: Dispersion ratio to cooling water
4-7) COOLING FAN DATA 1. Performance curves <P-Q>
∙ Part No. 15881-74110 (Applicable for DG972)
4-8) CENTER OF GRAVITY 1. With standard flywheel and rear-end plate
Center of gravity Model
Dry weight kg (lb)
X mm (in)
Y mm (in)
Z mm (in)
WG/DF972 72.0 (159)
-25.5 (-1.00)
73.3 (2.89)
179.5 (7.07)
2. With SAE flywheel and flywheel housing Center of gravity
Model Dry weight
kg (lb)
X mm (in)
Y mm (in)
Z mm (in)
DG972 -SAEH-S1
95.4 (210)
-10.0 (0.39)
28.0 (1.10)
207.0 (8.15)
Note Cooling water and lubricating oil weight is not included in above engine weight.
Flywheel end or flywheel housing end for SAE housing.
X
Y
Z
4-9) UNBALANCED FORCES OF ENGINES 1. Base data
2. Unbalanced inertia force and couple Model No. of Cylinder Cylinder Bore Order Fz Npy Noz
1 0 0.000096 0.000096WG/DF/DG972 3 74.5mm 2 0 0.000072 0
▼An example of calculation Fz, Npy, Noz Calculation condition ω2 Order Calculation
1 0 Fz 2 0 1 0.000096×142122=13.6kgNpy 2 0.000072×142122=10.2kg1 0.000096×142122=13.6kg
Engine model DG972
Engine speed 3600(rpm)
[2 x π x 3600/60]2 =142122
Noz 2 0
FZ: Unbalanced inertia force Npy, Noz: Unbalanced inertia couple mp: Reciprocating mass r: Crank radius l: Center distance of connecting rod L: Cylinder distance ω: Angular velocity
ω=2πn/60 n: Engine speed(rpm)
Cylinder bore (mm)
mp (kg)
l=0.098m r=0.0368mL=0.080m 74.5 0.37/9.80665
(xω2)
4-10) MASS ELASTIC SYSTEM Equivalent torsional vibration data
MODEL EQUIVALENT LENGTH (cm)
POLAR MOMENT OF INERTIA (kgfcm-sec2)
LV L1 L2 Lf JV J1 J2 J3 Jf DG972
-SAEH-S1 35082 4528 4528 2824 0.013 0.026 0.026 0.026 1.281
Note: Flywheel E8052-25110, V-Pulley 16861-74280
5. FUEL SYSTEM AND FUEL DIAGRAM • All fuel connections added to this engine must be installed by qualified personnel utilizing recognized procedures and standards.
• These non-KUBOTA installed parts, such as hoses, shutoff solenoid valve should be approved for Natural gas use.
• An approved, listed fuel filter and shutoff solenoid valve must be installed between the gas tank and Kubota regulator.
• Two fuel cut solenoids must be installed in series before the regulator on the fuel supply line for safety (backup) purpose.
1. Tightening torque and leak check 1) The joint must be installed to the gas entrance of the regulator by screw with O-ring.
Screw is tightened to the specified torque using a driver, and leak check must be performed as shown in the below table.
2) The connector on the gas mixer may be mounted on any position since it is not sealed. The lock nut may be loosened using a wrench. The connector may be changed to any specified angle. The lock nut should be tightened to the specified torque using a wrench as shown in the below table.
[ TIGHTENING TORQUE AND LEAK CHECK ] Tightening torque
Qty. Size Nm kgfm ft-lb Leak check pressure
SCREW 2 M4 1.9 to 2.9 0.2 to 0.3 1.5 to 2.2 LOCK NUT 1 M16×1 19.6 to 39.2 2.0 to 4.0 14.5 to 28.9
Soap solution or its equivalent
2. Setting of the regulator 1) Install the regulator in UPRIGHT position, it must be installed within 4G vibration level. If
not, it may not supply necessary fuel to the engine. 2) DO NOT connect any extension hose to the air vent pipe of the regulator. This may cause
an improper supply of fuel to the engine.
3. Caution for FUEL SYSTEM
The standard engine is equipped with φ6.6 jet for the fuel calorific gas value of 11000kcal/m3
(1236BTU/ft3). When the engine is operated with the different calorific gas, it is necessary to select the correct jet of the mixer. In that case, refer to the manual [ Adjustment for Natural Gas Engine DG972 ].
Japanese standard gas higher calorific value : 11000kcal/m3 (1236BTU/ft3)
supply pressure : 0.98 – 2.45kPa (7.35 – 18.38mmHg)
Equipments Vacuum Meter : Not KUBOTA supplied Adjustable Jet : Service Tool
4. Application Check Item
The items as shown below must be managed for all engines, and these items must be informed to KUBOTA with Application Check results. Refer to the attached sheet [ Application Check Sheet for DG972 ].
1) The diameter of the jet (with the intake vacuum curve) 2) The calorific value of the gas
3) The supply pressure of gas 4) The serial number of the engine
5. Fuel diagram
UPRIGHT position
Gas Mixer
Fuel Supply
Fuel filter
Shut off solenoids Two for safety (backup) purpose
Gas Regulator
Air Vent Pipe DO NOT connect any extension hose
Gas hose
Jet
NATURAL GAS ENGINE
DG972-E2PERFORMANCE CURVERATED POWER
KUBOTA DG SERIES (3-cylinder)
17.6kW@3600rpm
Photograph may show non-standard equipment.
FEATURES and BENEFITSNew Engine Series
The Kubota DG Series offers a new solution to the increasing needs for natural gas engine. The diesel engine based Kubota DG Series gives users the same foot-print, reliability and durability of D902, WG972, and DF972 acknowledged as the world's top quality small industrial engines.Kubota offers SAE Flywheel Housing and Rear End Plate specifications for the DG972 engine. These options offer users flexible Power Take Off (PTO) choices.The Kubota DG Series is designed to endure use outdoors under severe environment. This series is equipped with a bypass breather tube to avoid freezing below zero.
EmissionKubota DG Series complies with EPA Tier 2 Emissions Regulations. EPA regulation is one of the most stringent emissions regulations in the world.
Best Fuel SystemSpecialized for Natural Gas use, the DG972 engine eliminated the carburetor, regulator and a fuel filter parts, which are only necessary for Gasoline or LPG use. Also, Kubota adopts the best jet set and the ignition timing that provides the best engine performance in severe conditions.
Ease maintenance cost and timeMechanical governor system will contribute to lower maintenance cost and prevents users from having to deal with complicated electric maintenance. Moreover, water resistant spark plug caps are adopted for outdoor use.
2000 2400 2800 3200 3600
ENGINE SPEED [rpm]
Net Intermittent SAE J1349
BR
AK
E H
OR
SE
PO
WE
R
18
17
16
15
14
13
12
11
10
9
8
[ kW
]
[ HP
]
24
23
22
21
20
19
18
17
16
15
14
13
12
11
10
45
40
35
30
25
60
50
40
30
[ N. m
]
[ ft. l
b]
TO
RQ
UE
0.6
0.5
0.4
400
300
200
[ g/k
W. h
]
[ lb/H
P. h
]
SP
EC
IFIC
FU
EL
CO
NS
UM
PT
ION
KUBOTA Corporation
1334-01-COM ’08.09. .STD
2-47, Shikitsuhigashi 1-chome, Naniwa-ku, Osaka, 556-8601 JapanFax: 06-6648-3521 http://www.engine.kubota.co.jp
452.5 (17.81)
56.0 (2.20)
215.
0 (8
.46)
525.5 (20.69)
214.9 (8.46)
415.4 (16.35)
200.5 (7.89)
159.
0 (6
.26)
88.0(3.46)
502.
5 (1
9.78
)
88.0(3.46)
DG972-E2
GENERAL SPECIFICATION DIMENSIONS
*Specification is subject to change without notice. *Output: Net Intermittent SAE J1349*Dry weight is according to Kubota’s standard specification. When specification varies, the weight will vary accordingly.*1 with SAE Flywheel and Housing*2 with Rear End Plate
Model
Emission Regulation
Type
Number of Cylinders
Fuel
Intake System
Bore
Stroke
Displacement
mm (in)
mm (in)
L (cu.in)
Maximum Speed rpm
kW
hp
ps
Direction of Rotation
Oil Pan Capacity L (gal)
Starter Capacity V-kW
Alternator Capacity V-A
Length mm (in)
Width mm (in)
Height (1) mm (in)
Height (2) mm (in)
Dry Weight kg (lb)
DG972-E2
Tier 2
Vertical 4-cycle Liquid Cooled Natural Gas
3
74.5 (2.93)
73.6 (2.9)
0.962 (58.70)
Natural Gas
Naturally Aspirated
3600
17.6
23.6
23.9
Counterclockwise Viewed on Flywheel
3.7 (0.98)
12-1.0
12-40
525.5 (20.69)*1 / 452.5 (17.81)*2
415.4 (16.35)
502.5 (19.78)
159.0 (6.26)
72.0 (158.7)*1 / 95.4 (210.3)*2
KUBOTA DG SERIES
Output:Net Intermittent
Recommended